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<ep-patent-document id="EP07728185B1" file="EP07728185NWB1.xml" lang="en" country="EP" doc-number="2010550" kind="B1" date-publ="20130619" status="n" dtd-version="ep-patent-document-v1-4">
<SDOBI lang="en"><B000><eptags><B001EP>ATBECHDEDKESFRGBGRITLILUNLSEMCPTIESILTLVFIRO..CY..TRBGCZEEHUPLSK....IS..MT..........................</B001EP><B003EP>*</B003EP><B005EP>J</B005EP><B007EP>DIM360 Ver 2.40 (30 Jan 2013) -  2100000/0</B007EP></eptags></B000><B100><B110>2010550</B110><B120><B121>EUROPEAN PATENT SPECIFICATION</B121></B120><B130>B1</B130><B140><date>20130619</date></B140><B190>EP</B190></B100><B200><B210>07728185.5</B210><B220><date>20070417</date></B220><B240><B241><date>20080812</date></B241><B242><date>20111128</date></B242></B240><B250>en</B250><B251EP>en</B251EP><B260>en</B260></B200><B300><B310>06112984</B310><B320><date>20060424</date></B320><B330><ctry>EP</ctry></B330></B300><B400><B405><date>20130619</date><bnum>201325</bnum></B405><B430><date>20090107</date><bnum>200902</bnum></B430><B450><date>20130619</date><bnum>201325</bnum></B450><B452EP><date>20130107</date></B452EP></B400><B500><B510EP><classification-ipcr sequence="1"><text>C07F  11/00        20060101AFI20080123BHEP        </text></classification-ipcr><classification-ipcr sequence="2"><text>C07F   7/00        20060101ALI20080123BHEP        </text></classification-ipcr></B510EP><B540><B541>de</B541><B542>POLYMERISIERUNG VON ETHYLEN UND ALPHA-OLEFINEN MIT PYRIDINO-IMINOPHENOL-KOMPLEXEN</B542><B541>en</B541><B542>POLYMERISATION OF ETHYLENE AND ALPHA-OLEFINS WITH PYRIDINO-IMINOPHENOL COMPLEXES</B542><B541>fr</B541><B542>POLYMÉRISATION D'ÉTHYLÈNE ET D'ALPHA-OLÉFINES AVEC DES COMPLEXES PYRIDINO-IMINOPHÉNOL</B542></B540><B560><B561><text>EP-A- 1 574 529</text></B561><B561><text>EP-A2- 0 717 103</text></B561><B562><text>MATSUI, S. ET AL.: "FI Catalysts: super active new ethylene polymerization catalysts" CATALYSIS TODAY, no. 66(1), 2001, pages 63-73, XP002438748 &amp; DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; MATSUI, S. ET AL: "FI Catalysts: super active new ethylene polymerization catalysts" XP002405857 retrieved from STN Database accession no. 2001:246353</text></B562><B562><text>DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; KOPRIVANAC, N. ET AL: "The structures of the chosen metal complexes with 2-[(2-quinolylmethylene)amino]phenol (QMAP) as a ligand" XP002405854 retrieved from STN Database accession no. 1997:217038 &amp; SPECTROSCOPY LETTERS , 30(2), 181-192 CODEN: SPLEBX; ISSN: 0038-7010, 1997,</text></B562><B562><text>DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; DURAN, M. L. ET AL: "Complexes formed in the interaction of titanium tetrachloride with Schiff bases derived from 2-pyridinealdehyde and 2-aminophenols" XP002405855 retrieved from STN Database accession no. 1988:562255 &amp; ANALES DE QUIMICA, SERIE B: QUIMICA INORGANICA Y QUIMICA ANALITICA , 84(1), 60-4 CODEN: AQSAD3; ISSN: 0211-1349, 1988,</text></B562><B562><text>DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; JIMENEZ RUEDAS, M. ET AL: "Study of the solid complexes formed by 1-picolylideneamino-2- naphthol with nickel(II) and cobalt(II)" XP002405856 retrieved from STN Database accession no. 1980:596836 &amp; AFINIDAD , 37(366), 133-6 CODEN: AFINAE; ISSN: 0001-9704, 1980,</text></B562><B562><text>BACCHI, ALESSIA ET AL: "Potentially tridentate ligands in the synthesis of methyl- and acetylpalladium(II) complexes" EUROPEAN JOURNAL OF INORGANIC CHEMISTRY , (8), 2179-2187 CODEN: EJICFO; ISSN: 1434-1948, 2002, XP002405847 cited in the application</text></B562><B562><text>DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; PACHON, LAURA DURAN ET AL: "Intramolecular oxidation of the ligand 4-methyl-2-N-(2- pyridylmethyl)aminophenol (Hpyramol) upon coordination with iron(II) chloride and manganese(II) perchlorate" XP002405858 retrieved from STN Database accession no. 2004:730105 &amp; INORGANICA CHIMICA ACTA , 357(12), 3697-3702 CODEN: ICHAA3; ISSN: 0020-1693, 2004,</text></B562><B562><text>DATABASE CA [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; BAMFIELD, P. ET AL: "Five-coordinate complexes of bivalent iron, cobalt, nickel, copper, and zinc halides with terdentate Schiff base and azo ligands containing tertiary nitrogen donor atoms" XP002405859 retrieved from STN Database accession no. 1969:418382 &amp; JOURNAL OF THE CHEMICAL SOCIETY [SECTION] A: INORGANIC, PHYSICAL, THEORETICAL , (9), 1447-52 CODEN: JCSIAP; ISSN: 0022-4944, 1969,</text></B562></B560></B500><B700><B720><B721><snm>HILLAIRET, Caroline</snm><adr><str>Rue du Nouveau Monde, 64</str><city>7060 Soignies</city><ctry>BE</ctry></adr></B721><B721><snm>MICHAUD, Guillaume</snm><adr><str>13 rue des Canonniers</str><city>59000 Lille</city><ctry>FR</ctry></adr></B721><B721><snm>SIROL, Sabine</snm><adr><str>rue I. Vanschepdael 37</str><city>1440 Wauthier-Braine</city><ctry>BE</ctry></adr></B721></B720><B730><B731><snm>TOTAL RESEARCH &amp; TECHNOLOGY FELUY</snm><iid>101324976</iid><irf>F-996 EPT</irf><adr><str>Zone Industrielle C</str><city>7181 Seneffe</city><ctry>BE</ctry></adr></B731></B730></B700><B800><B840><ctry>AT</ctry><ctry>BE</ctry><ctry>BG</ctry><ctry>CH</ctry><ctry>CY</ctry><ctry>CZ</ctry><ctry>DE</ctry><ctry>DK</ctry><ctry>EE</ctry><ctry>ES</ctry><ctry>FI</ctry><ctry>FR</ctry><ctry>GB</ctry><ctry>GR</ctry><ctry>HU</ctry><ctry>IE</ctry><ctry>IS</ctry><ctry>IT</ctry><ctry>LI</ctry><ctry>LT</ctry><ctry>LU</ctry><ctry>LV</ctry><ctry>MC</ctry><ctry>MT</ctry><ctry>NL</ctry><ctry>PL</ctry><ctry>PT</ctry><ctry>RO</ctry><ctry>SE</ctry><ctry>SI</ctry><ctry>SK</ctry><ctry>TR</ctry></B840><B860><B861><dnum><anum>EP2007053720</anum></dnum><date>20070417</date></B861><B862>en</B862></B860><B870><B871><dnum><pnum>WO2007122139</pnum></dnum><date>20071101</date><bnum>200744</bnum></B871></B870><B880><date>20090107</date><bnum>200902</bnum></B880></B800></SDOBI>
<description id="desc" lang="en"><!-- EPO <DP n="1"> -->
<p id="p0001" num="0001">The present invention relates to the field of single site catalyst systems based on pyridine-iminophenol, pyridine-iminoalcohol or pyridine-iminoamine complexes and suitable for oligomerising or polymerising ethylene and alpha-olefins.</p>
<p id="p0002" num="0002">A multitude of catalyst systems available for polymerising or oligomerising ethylene and alpha-olefins exist, but there is a growing need for finding new systems capable of tailoring polymers with very specific properties. More and more post-metallocene catalyst components based on early or late transition metals from Groups 3 to 10 of the Periodic Table have recently been investigated such as for example those disclosed in Gibson and al. review (<nplcit id="ncit0001" npl-type="s"><text>Gibson, V.C.; Spitzmesser, S.K., in Chem. Rev. 2003, 103, p. 283</text></nplcit>).</p>
<p id="p0003" num="0003">Pyridine-iminophenol derivatives are known and have been described for example by Ismet et al. (<nplcit id="ncit0002" npl-type="s"><text>Ismet, K.; Fatma, M.; Dig Dem E. in Journal of Polymer Science: Part A: Polymer Chemistry, Vol. 42, 2717-2724, 2004</text></nplcit>) or by Asada et al. (<nplcit id="ncit0003" npl-type="s"><text>Asada, H.; Hayashi, K.; Negoro, S.; Fujiwara, M.; Matsushita, T. in Inorganic Chemistry Communications 6, 193-196, 2003</text></nplcit>) or by Bacchi et al. (<nplcit id="ncit0004" npl-type="s"><text>Bacchi, A.; Carcelli, M.; Pelizzi,C.; Pelizzi, G.; Pelagatti, P.; Ugolotti, S. in Eur. J. lnorg. Chem. 2179-2187, 2002</text></nplcit>), but corresponding complexes have never been described as catalysts for the polymerisation of olefins.</p>
<p id="p0004" num="0004">Matsui and Fujita (<nplcit id="ncit0005" npl-type="s"><text>Matsui S. and Fujita T. in Catalysis Today, 2001, 66, 63-73</text></nplcit>) disclose the synthesis of ligand-oriented group 4-based catalyst components having two phenoxy-imine ligands. These were also tested in the polymerisation of ethylene at atmospheric pressure with methylaluminoxane as cocatalyst. Some exhibited fair to high activity and some displayed practically no activity.</p>
<p id="p0005" num="0005">There is still a need to improve either the specificities or the performances of these systems.<!-- EPO <DP n="2"> --></p>
<p id="p0006" num="0006">It is an aim of this invention to provide new single site catalysts based on tridentate pyridine-iminophenol, pyridine-iminoalcohol or pyridine-iminoamine.</p>
<p id="p0007" num="0007">It is another aim of the present invention to provide active catalyst systems based on these catalyst components.</p>
<p id="p0008" num="0008">It is a further aim of the present invention to provide a process for polymerising or for oligomerising ethylene and alpha-olefins with these new catalyst systems.</p>
<p id="p0009" num="0009">Any one or more of these aims is fulfilled, at least partially, by the present invention.</p>
<p id="p0010" num="0010">Accordingly, the present invention discloses metallic complexes of formula I
<chemistry id="chem0001" num="0001"><img id="ib0001" file="imgb0001.tif" wi="62" he="66" img-content="chem" img-format="tif"/></chemistry>
wherein R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, and R<sub>9</sub> are each independently selected from hydrogen, unsubstituted or substituted hydrocarbyl having from 1 to 20 carbon atoms, or inert functional group and two or more of those groups can themselves be linked together to form further ring or rings, with the restriction that at least one of R<sub>1</sub>, R<sub>7</sub> and R<sub>8</sub> is not hydrogen;<br/>
wherein M is a metal Group 3 to 10 of the Periodic Table;<br/>
<!-- EPO <DP n="3"> -->wherein Y is ○ or NR*, with R* being alkyl or aryl group having from 1 to 12 carbon atoms;<br/>
wherein each X can be the same or different and is selected from halogen, substituted or unsubstituted hydrocarbyl having from 1 to 20 carbon atoms, substituted or unsubstituted aryloxy or alkoxy;<br/>
wherein m is zero or an integer from 1 to 3; and<br/>
wherein (n+1) is the valence of M.</p>
<p id="p0011" num="0011">The metallic complex results from the complexation of a ligand of general formula II with metallic salt MX<sub>n+1</sub> in a solvent
<chemistry id="chem0002" num="0002"><img id="ib0002" file="imgb0002.tif" wi="64" he="77" img-content="chem" img-format="tif"/></chemistry>
wherein R<sub>1</sub> to R<sub>9</sub> are as described hereabove.</p>
<p id="p0012" num="0012">Ligand of formula II is the reaction product of carbonylated pyridine of formula III with compound of formula IV,<!-- EPO <DP n="4"> -->
<chemistry id="chem0003" num="0003"><img id="ib0003" file="imgb0003.tif" wi="45" he="47" img-content="chem" img-format="tif"/></chemistry>
<chemistry id="chem0004" num="0004"><img id="ib0004" file="imgb0004.tif" wi="52" he="48" img-content="chem" img-format="tif"/></chemistry>
wherein R<sub>1</sub> to R<sub>9</sub> are as described hereabove.</p>
<p id="p0013" num="0013">The reaction conditions are well known in the art.</p>
<p id="p0014" num="0014">By inert functional group, is meant a group, other than hydrocarbyl or substituted hydrocarbyl, that is inert under the complexation conditions to which the compound containing said group is subjected. They can be selected for example from halo, ester, ether, amino, imino, nitro, cyano, carboxyl, phosphate, phosphonite, phosphine, phosphinite, thioether and amide. Preferably, they are selected from halo, such as chloro, bromo, fluoro and iodo, or ether of formula - OR* wherin R* is unsubstituted or substituted hydrocarbyl. After metallation of the ligand, an inert functional group must not coordinate to the metal more strongly than the groups organised to coordinate to the metal and thereby displace the desired coordinating group.<!-- EPO <DP n="5"> --></p>
<p id="p0015" num="0015">In preferred embodiments according to the present invention, m is zero and R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, and R<sub>9</sub> are hydrogen and R<sub>1</sub>, R<sub>7</sub> and R<sub>8</sub>, can each be independently selected from hydrogen, substituted or unsubstituted hydrocarbyl having from 1 to 20 carbon atoms, halogen, nitro or cyano groups, with the restriction that at least one of them is not hydrogen.</p>
<p id="p0016" num="0016">In this description, substituted hydrocarbyls are defined as chains or links that may comprise one or more heteroatoms.</p>
<p id="p0017" num="0017">Some precursors for R<sub>1</sub> can advantageously be selected from aromatic or heteroaromatic boronic acids of formula
<chemistry id="chem0005" num="0005"><img id="ib0005" file="imgb0005.tif" wi="30" he="33" img-content="chem" img-format="tif"/></chemistry>
wherein each R' is independently selected from hydrogen or hydrocarbyl or inert functional group.</p>
<p id="p0018" num="0018">Other precursors for R<sub>1</sub> can be selected from any one of the following:
<chemistry id="chem0006" num="0006"><img id="ib0006" file="imgb0006.tif" wi="92" he="34" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="6"> -->
<chemistry id="chem0007" num="0007"><img id="ib0007" file="imgb0007.tif" wi="123" he="32" img-content="chem" img-format="tif"/></chemistry>
<chemistry id="chem0008" num="0008"><img id="ib0008" file="imgb0008.tif" wi="135" he="60" img-content="chem" img-format="tif"/></chemistry>
<chemistry id="chem0009" num="0009"><img id="ib0009" file="imgb0009.tif" wi="139" he="29" img-content="chem" img-format="tif"/></chemistry>
<chemistry id="chem0010" num="0010"><img id="ib0010" file="imgb0010.tif" wi="111" he="24" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0019" num="0019">Preferably, R<sub>1</sub>, R<sub>7</sub>, and R<sub>8</sub> are each independently selected from hydrogen or substituted or unsubstituted alkyl or aryl groups or halogen with the restriction that at least one of them is not hydrogen.</p>
<p id="p0020" num="0020">The preferred alkyl groups are methyl and tert-butyl.<br/>
The preferred aryl groups are unsubstituted or substituted phenyl groups.<br/>
The preferred halogen is chlorine.</p>
<p id="p0021" num="0021">Preferably all three R<sub>1</sub>, R<sub>7</sub> and R<sub>8</sub> are not hydrogen simultaneously.<!-- EPO <DP n="7"> --></p>
<p id="p0022" num="0022">More preferably either R<sub>7</sub> or R<sub>8</sub> is present, the other being hydrogen and R<sub>1</sub> is one of the preferred substituent groups or hydrogen.</p>
<p id="p0023" num="0023">Preferably M is Ti, Zr, Hf, V, Cr, Mn, Fe, Co, Ni, Pd or rare earths. More preferably, it is Ti, Cr, Fe or Zr.</p>
<p id="p0024" num="0024">Preferably X is halogen, more preferably it is chlorine.</p>
<p id="p0025" num="0025">The solvent may be selected from dichloromethane or tetrahydrofuran and the complexation reaction is carried out at room temperature or at reflux.</p>
<p id="p0026" num="0026">The present invention further discloses an active catalyst system comprising the single site catalyst component of formula I and an activating agent having an ionising action.</p>
<p id="p0027" num="0027">Suitable activating agents are well known in the art. The activating agent can be an aluminium alkyl represented by formula AlR<sup>+</sup><sub>n</sub>X<sub>3-n</sub> wherein R<sup>+</sup> is an alkyl having from 1 to 20 carbon atoms and X is a halogen. The preferred alkylating agents are triisobutyl aluminium (TIBAL) or triethyl aluminium (TEAL).</p>
<p id="p0028" num="0028">Alternatively, it can be aluminoxane and comprise oligomeric linear and/or cyclic alkyl aluminoxanes represented by formula
<chemistry id="chem0011" num="0011"><img id="ib0011" file="imgb0011.tif" wi="35" he="19" img-content="chem" img-format="tif"/></chemistry>
for oligomeric, linear aluminoxanes and by formula
<chemistry id="chem0012" num="0012"><img id="ib0012" file="imgb0012.tif" wi="19" he="19" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="8"> -->
for oligomeric, cyclic aluminoxane,<br/>
wherein n is 1-40, preferably 10-20, m is 3-40, preferably 3-20 and R* is a C<sub>1</sub>-C<sub>8</sub> alkyl group and preferably methyl.</p>
<p id="p0029" num="0029">Preferably, the activating agent is methylaluminoxane (MAO) or tetra-isobutyldialuminoxane (IBAO), more preferably, it is IBAO.</p>
<p id="p0030" num="0030">The amount of activating agent is selected to give an Al/M ratio of from 100 to 3000, preferably of from 500 to 2000. The amount of activating agent depends upon its nature: for IBAO the preferred Al/M ratio is of about 500, and for MAO, it is about 2000.</p>
<p id="p0031" num="0031">Suitable boron-containing activating agents may comprise a triphenylcarbenium boronate such as tetrakis-pentafluorophenyl-borato-triphenylcarbenium as described in <patcit id="pcit0001" dnum="EP0427696A"><text>EP-A-0427696</text></patcit>, or those of the general formula [L'-H] + [B Ar<sub>1</sub> Ar<sub>2</sub> X<sub>3</sub> X<sub>4</sub>]- as described in <patcit id="pcit0002" dnum="EP0277004A"><text>EP-A-0277004</text></patcit> (page 6, line 30 to page 7, line 7). The amount of boron -containing activating agent is selected to give B/M ratio of from 0.5 to 5, preferably of about 1.</p>
<p id="p0032" num="0032">In another embodiment, according to the present invention, the single site catalyst component of formula I may be deposited on a conventional support. Preferably, the conventional support is silica impregnated with MAO. Alternatively and preferably, it can be an activating support such as fluorinated alumina silica.</p>
<p id="p0033" num="0033">The present invention further discloses a method for preparing an active catalyst system that comprises the steps of:
<ol id="ol0001" compact="compact" ol-style="">
<li>a) providing a ligand of formula II;</li>
<li>b) complexing the ligand of step a) with a metallic salt Man+1 in a solvent;</li>
<li>c) retrieving catalyst component I;</li>
<li>d) activating with an activating agent having an ionising action;</li>
<li>e) optionally adding a cocatalyst;</li>
<li>f) retrieving an active oligomerisation or polymerisation catalyst system.</li>
</ol><!-- EPO <DP n="9"> --></p>
<p id="p0034" num="0034">Alternatively, in step d) catalyst component I is deposited on a support impregnated with an activating agent or on an activating support containing fluor.</p>
<p id="p0035" num="0035">The cocatalyst may be selected from triethylaluminium, triisobutylaluminum, tris-n-octylaluminium, tetraisobutyldialuminoxane or diethyl zinc.</p>
<p id="p0036" num="0036">The active catalyst system is used in the oligomerisation and in the polymerisation of ethylene and alpha-olefins.</p>
<p id="p0037" num="0037">The present invention discloses a method for the oligomerisation or the homo-or co-polymerisation of ethylene and alpha-olefins that comprises the steps of:
<ol id="ol0002" compact="compact" ol-style="">
<li>a) injecting the active catalyst system into the reactor; and</li>
<li>b) injecting the monomer and optional comonomer either before or after or simultaneously with step a);</li>
<li>c) maintaining under polymerisation conditions;</li>
<li>d) retrieving the oligomers and/or polymer.</li>
</ol></p>
<p id="p0038" num="0038">The pressure in the reactor can vary from 0.5 to 50 bars, preferably from 5 to 25 bars.</p>
<p id="p0039" num="0039">The polymerisation temperature can range from 10 to 100°C, preferably from 50 to 85°C.</p>
<p id="p0040" num="0040">Preferably the monomer and optional comonomer are selected from ethylene, propylene or 1-hexene.</p>
<p id="p0041" num="0041">In another preferred embodiment according to the present invention, the optional comonomer is a polar functionalised alpha-olefin.</p>
<heading id="h0001"><u><b>List of</b> Figures.</u></heading><!-- EPO <DP n="10"> -->
<p id="p0042" num="0042">
<ul id="ul0001" list-style="none">
<li><figref idref="f0001">Figure 1</figref> represents the Gel Permeation Chromatography (GPC) curve of the polyethylene resin obtained with catalyst D7 activated with IBAO, with iC4 as solvent, at a temperature of 85 °C, under an ethylene pressure of 29 bars and after a polymerisation time of 30 minutes.</li>
<li><figref idref="f0002">Figure, 2</figref> represents the GPC curve of the polyethylene resin obtained with catalyst D1 activated with IBAO, with iC4 as solvent, at a temperature of 85 °C, under an ethylene pressure of 24 bars and after a polymerisation time of 30 minutes.</li>
<li><figref idref="f0002">Figure 3</figref> represents the GPC curve of the polyethylene resin obtained with catalyst D7 activated with TiBAI, with iC4 as solvent and hexene as comonomer at a temperature of 85 °C, under an ethylene pressure of 24 bars and after a polymerisation time of 60 minutes.</li>
<li><figref idref="f0003">Figure 4</figref> represents the GPC curve of the polyethylene resin obtained with catalyst D1 activated with IBAO, with heptane as solvent, at a temperature of 85 °C, under an ethylene pressure of 22 bars and after a polymerisation time of 30 minutes.</li>
</ul></p>
<heading id="h0002"><b><u>Examples.</u></b></heading>
<p id="p0043" num="0043">All reactions were performed using standard Schlenk techniques or in an argon-filled glove-box. The starting materials and reagents, purchased from commercial suppliers, were used without purification. All the solvents were dried and distilled before use either over sodium and benzophenone for toluene, pentane and THF, or over CaH<sub>2</sub> for ethanol. <sup>1</sup>H, <sup>13</sup> C and <sup>31</sup>P NMR spectra were recorded on a Bruker Advance300 apparatus.</p>
<heading id="h0003"><b><u>Preparation of ligands.</u></b></heading>
<heading id="h0004"><b><u>I. Precursors</u></b></heading><!-- EPO <DP n="11"> -->
<heading id="h0005"><b><u>Synthesis of precursor [6-phenyl]-2-pyridinecarboxaldehyde (A).</u></b></heading>
<p id="p0044" num="0044">192 mg (1 mmol) of 6-bromo-2-pyridinecarboxaldehyde and 152 mg (1.2 mmol) of phenylboronic acid were dissolved in 10 mL of tetrahydrofuran (THF). 1 ml (1mmol) of Na<sub>2</sub>CO<sub>3</sub> in aqueous solution (1M) and 8 mg (0.7%) of Pd(PPh<sub>3</sub>)<sub>4</sub> were added. The reaction mixture was heated during 45 min, at a temperature of 130°C in a micro-wave reactor. The solution was filtered on paper, 10 ml of AcOEt were added and the organic phase was successively washed with NaHCO<sub>3</sub>, with H<sub>2</sub>O and with an aqueous solution of NaCl. The organic phase was dried over MgSO<sub>4</sub>, filtered and evaporated to dryness. After a chromatography on silica gel (Pentane/Et<sub>2</sub>O, 1/1), 136 mg of aldehyde A were obtained as colourless oil with a yield of 74%.
<chemistry id="chem0013" num="0013"><img id="ib0013" file="imgb0013.tif" wi="30" he="27" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 10.17 (s, 1 H), 8.11 (d, J=6Hz, 2H), 7.89 (m, 3H), 7.49 (m, 3H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 114.5, 119.2, 121.8, 123.7, 124.4, 132.5, 132.8, 147.5, 188.7.</p>
<heading id="h0006"><b><u>Synthesis of precursor [6-(2-phenyl)phenyl]-2-pyridinecarboxaldehyde (B).</u></b></heading>
<p id="p0045" num="0045">Precursor (B) was prepared following the same procedure as that used to prepare precursor (A) except that 238 mg (1.2 mmol) of (2-phenyl)phenylboronic acid were used as reagent. 255 mg of precursor (B) were obtained as colourless oil with a yield of 98%.<!-- EPO <DP n="12"> -->
<chemistry id="chem0014" num="0014"><img id="ib0014" file="imgb0014.tif" wi="30" he="35" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 10.09 (s, 1H), 7.79 (d, J=6Hz, 2H), 7.52 (m, 4H), 7.25 (m, 3H), 7.15 (m, 3H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 119.2, 127.0, 127.9, 128.2, 129.1, 129.5, 129.7, 130.7, 135.0, 136.1, 138.2, 140.9, 152.5, 159.9, 193.7.</p>
<heading id="h0007"><b><u>Synthesis of precursor [6-(2,6-dimethylphenyl)]-2-pyridinecarboxaldehyde (C).</u></b></heading>
<p id="p0046" num="0046">Precursor (C) was prepared following the same procedure as that used to prepare precursor (A) except that 180 mg (1.2 mmol) of 2,6-(dimethyl)phenylboronic acid were used as reagent. 200 mg of precursor (C) were obtained as colourless oil with a yield of 95%.
<chemistry id="chem0015" num="0015"><img id="ib0015" file="imgb0015.tif" wi="30" he="27" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 10.13 (s, 1H), 7.96 (d, J=6Hz, 2H), 7.48 (m, 1H), 7.25 (m, 1H), 6.99 (d, J=6Hz, 2H), 2.06 (s, 6H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 15.0, 114.3, 121.5, 122.6, 123.2, 123.7, 132.1, 147.6, 188.6.</p>
<heading id="h0008"><b><u>Synthesis of precursor [6-naphthyl]-2-pyridinecarboxaldehyde (D).</u></b></heading>
<p id="p0047" num="0047">Precursor (D) was prepared following the same procedure as that used to prepare precursor (A) except that 206 mg (1.2 mmol) of 2-naphthylboronic acid were used as reagent. 190 mg of precursor (D) were obtained as colourless oil with a yield of 82%.<!-- EPO <DP n="13"> -->
<chemistry id="chem0016" num="0016"><img id="ib0016" file="imgb0016.tif" wi="35" he="26" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, COCl<sub>3</sub>) δ (ppm): 10.21 (s, 1H), 8.01 (m, 5H), 7.80 (d, J=6Hz, 1 H), 7.55 (m, 4H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 114.6, 120.0, 120.1, 120.9, 121.6, 122.5,123.3,124.0,124.3,128.7,132.0,132.3, 148.0, 154.7, 188.6.</p>
<heading id="h0009"><b><u>Synthesis of Precursor [6-(2-methoxyphenyl)]-2-pyridinecarboxaldehyde (E)</u>.</b></heading>
<p id="p0048" num="0048">Precursor (E) was prepared following the same procedure as that used to prepare precursor (A) except that 376 mg (2.4 mmol) of 2-methylphenylboronic acid were used as reagent. 425 mg of precursor (E) were obtained as colourless oil with a yield of 98%.
<chemistry id="chem0017" num="0017"><img id="ib0017" file="imgb0017.tif" wi="30" he="26" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 3.90 (s, 3H), 7.06 (d, J=2.1 Hz, 1H). 7.15 (t, J=2.0Hz, 1H), 7.45 (dt, J= 2Hz and J=0.4Hz, 1H), 7.91 (m, 3H), 8.11 (dd, J=1.6Hz and J=0.7Hz, 1 H), 10.2 (s, 1H).</p>
<heading id="h0010"><b><u>Synthesis of precursor [6-(quinolin-8-yl)]-2-pyridinecarboxaldehyde (F).</u></b></heading>
<p id="p0049" num="0049">Precursor (F) was prepared following the same procedure as that used to prepare precursor (A) except that 216 mg (1.2 mmol) of 8-quinolineboronic acid were used as reagent. 232 mg of precursor (F) were obtained as pale yellow solid with a yield of 99%.<!-- EPO <DP n="14"> -->
<chemistry id="chem0018" num="0018"><img id="ib0018" file="imgb0018.tif" wi="31" he="33" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 7.49 (dd, J=2.0Hz and J=1.0Hz, 1H), 7.74 (t, J=2.0Hz, 1H), 7.96 (d, J=2.0Hz, 1H), 8.01 (m, 2H), 8.27 (d, J=2.0Hz, 2H), 8.41 (m, 1 H), 8.98 (dd, J=1.0Hz and J=0.4Hz, 1 H), 10.22 (s, 1H).</p>
<heading id="h0011"><b><u>Synthesis of precursor [6-(2-trifluoromethyl)]-2-pridinecarboxaldehyde (G)</u>.</b></heading>
<p id="p0050" num="0050">Precursor (G) was prepared following the same procedure as that used to prepare precursor (A) except that 470 mg (2.4 mmol) of 2-trifluoromethylphenylboronic acid were used as reagent. 477 mg of precursor (G) were obtained as orange oil with a yield of 95%.
<chemistry id="chem0019" num="0019"><img id="ib0019" file="imgb0019.tif" wi="30" he="27" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 7.57 (dt, J=2.0Hz and J=0.4Hz, 2H), 7.67 (dd, J=1.6Hz and J=0.4Hz, 2H), 7.83 (d, J=1.8Hz, 1H), 7.99 (m, 2H), 10.12 (s, 1 H).</p>
<heading id="h0012"><b><u>Synthesis of precursor [6-(4-dibenzofuran)]2-pyridinecarboxaldehyde (H).</u></b></heading>
<p id="p0051" num="0051">Precursor (H) was prepared following the same procedure as that used to prepare precursor (A) except that 524 mg (2.4 mmol) of dibenzofuran-4-boronic acid were used as reagent. 540 mg of precursor (H) were obtained as pale yellow solid with a yield of 99%.<!-- EPO <DP n="15"> -->
<chemistry id="chem0020" num="0020"><img id="ib0020" file="imgb0020.tif" wi="30" he="40" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 7.42 (t, J=2.0Hz, 1H), 7.54 (q, J=1.9Hz, 2H), 7.67 (d, J=1.9Hz, 1H), 8.00 (t, J=2.0Hz, 2H), 8.06 (m, 2H), 8.49 (d, J=2.0Hz, 1H), 8.73 (d, J=2.0Hz, 1H), 10.24 (s, 1H).</p>
<heading id="h0013"><b><u>II. Ligands.</u></b></heading>
<heading id="h0014"><b><u>Synthesis of ligand 2-[(2-pyridyl)-methylimino]-phenol (L1)</u><sub><u>.</u></sub></b></heading>
<p id="p0052" num="0052">200 µl (2 mmol) of 2-pyridinecarboxaldehyde (reagent 1) and 220 mg (2 mmol) of 2-aminophenol (reagent 2) were dissolved in 10 mL of dry ethanol. One drop of glacial acetic acid was added and the reaction mixture was stirred during 12 h. The solution was filtered on paper and the filtrate was evaporated to dryness. After a chromatography on silica gel (CH<sub>2</sub>Cl<sub>2</sub>, 100 ml then AcOEt 200 ml), 394 mg of ligand L1 were obtained as orange solid with a yield of 100%.
<chemistry id="chem0021" num="0021"><img id="ib0021" file="imgb0021.tif" wi="29" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.83 (s, 1 H), 8.72 (d, J=6Hz, 1H), 8.17 (d, J=9Hz, 1H), 7.83 (t, J=6Hz, 1H), 7.38 (m, 2H), 7.22 (d, J=9<sub>Hz</sub>, 1H), 7.03 (d, J=9Hz, 1 H), 6.95 (t, J=9Hz, 1 H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 115.4, 116.1, 120.2, 121.8, 125.2, 129.9, 134.5, 136.8, 149.7, 152.8, 154.1, 156.7.<!-- EPO <DP n="16"> --></p>
<heading id="h0015"><u>Synthesis of ligand 2-phenyl-2-(pyridylmethyleneamino)ethanol (L2)</u></heading>
<p id="p0053" num="0053">Ligand L2 was prepared following the same procedure as that used to prepare ligand L1 except that 200 µl (2 mmol) of 2-phenylglycinol were used as reagent 2. 196 mg of ligand L2 were obtained yellow oil with a yield of 43 %.
<chemistry id="chem0022" num="0022"><img id="ib0022" file="imgb0022.tif" wi="34" he="36" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0054" num="0054"><sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 8.58 (m, 1H), 8.44 (s, 1 H), 8.00 (d, J=9Hz, 1H), 7.70 (t, J=9Hz, 1H), 7.40-7.26 (m, 6H), 4.53 (m, 1H), 3.90-3.63 (m, 2H), 2.90 (bs, 1 H).</p>
<heading id="h0016"><b><u>Synthesis of ligand 2-[(2-pyridyl)-methylimino]-4-methyl-phenol (L3).</u></b></heading>
<p id="p0055" num="0055">Ligand L3 was prepared following the same procedure as that used to prepare ligand L1 except that 635 mg (5 mmol) of 2-amino-4-methyl-phenol were used as reagent 2. 850 mg of ligand L3 were obtained as yellow-green solid with a yield of 80 %.
<chemistry id="chem0023" num="0023"><img id="ib0023" file="imgb0023.tif" wi="34" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.82 (s, 1H), 8.73 (d, J=6Hz, 1H), 8.19 (d, J=9Hz, 1H), 7.83 (t, J=6Hz, 1H), 7.40 (m, 1H), 7.20 (s, 1 H), 7.05 (d, J=9Hz, 1 H), 6.92 (d, J=9Hz, 1 H), 2.31 (s, 3H)<br/>
<sup>13</sup>C(<sup>1</sup>H) NMR (75 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 21.0, 115.5, 117.4, 122.0, 125.7, 130.1, 130.9, 134.9, 137.1, 150.3, 151.1, 155.0, 157.8.<!-- EPO <DP n="17"> --></p>
<heading id="h0017"><u>Synthesis of ligand 2-[(2-pyridyl)-methyliminol-5-methyl-phenol (L4).</u></heading>
<p id="p0056" num="0056">Ligand L4 was prepared following the same procedure as that used to prepare ligand L1 except that 628 mg (5 mmol) of 2-amino-5-methyl-phénol were used as reagent 2. 928 mg of ligand L4 were obtained as light brown solid with a yield of 87 %.
<chemistry id="chem0024" num="0024"><img id="ib0024" file="imgb0024.tif" wi="34" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0057" num="0057"><sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.81 (s, 1H), 8.71 (d, J=6Hz, 1H), 8.18 (d, J=9Hz, 1H), 7.81 (t, J=6Hz, 1H), 7.37 (m, 1H), 7.31 (d, J=9Hz, 1H), 6.86 (s, 1H), 6.73 (d, J=9Hz, 1 H), 2.35 (s, 3H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CD<sub>2</sub>Cl<sub>2</sub>)□ δ (ppm): 21.8, 116.2, 116.4, 121.6, 122.0, 125.6, 132.7, 137.2, 141.2, 150.3, 153.3, 155.1, 156.6.</p>
<heading id="h0018"><b><u>Synthesis of ligand 2-[(2-pyridyl)methylimino]-4-tertbutyl-phenol (L5).</u></b></heading>
<p id="p0058" num="0058">Ligand L5 was prepared following the same procedure as that used to prepare ligand L1 except that 852 mg (5 mmol) of 2-amino-4-tertbutyl-phénol were used as reagent 2. 1353 mg of ligand L5 were obtained as yellow-green solid with a yield of 99 %.
<chemistry id="chem0025" num="0025"><img id="ib0025" file="imgb0025.tif" wi="39" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0059" num="0059"><sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.88 (s, 1H), 8.72 (d, J=6Hz, 1H), 8.21 (d, J=9Hz, 1H), 7.83 (t, J=6Hz, 1H), 7.43 (d, J=6Hz, 1H), 7.39 (m, 1H), 7.30 (d, J=9Hz, 1 H), 7.12 (bs, 1H), 6.97 (d, J=9Hz, 1 H), 1.33 (s, 9H)<br/>
<!-- EPO <DP n="18"> --><sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CD<sub>2</sub>Cl<sub>2</sub>)□ δ (ppm): 31.8, 34.8, 113.7, 115.1, 121.9, 125.7, 127.5, 129.3, 134.5, 137.1, 143.8, 150.3, 150.9, 157.8.</p>
<heading id="h0019"><b><u>Synthesis of ligand 2-[(2-pyridyl)methylimino]-4-phenyl-phenol (L6).</u></b></heading>
<p id="p0060" num="0060">Ligand L6 was prepared following the same procedure as that used to prepare ligand L1 except that 1029 mg (5 mmol) of 2-amino-3-methyl-phénol were used as reagent 2. 1355 mg of ligand L6 were obtained as brown-red solid with a yield of 99 %.
<chemistry id="chem0026" num="0026"><img id="ib0026" file="imgb0026.tif" wi="43" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0061" num="0061"><sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.94 (s, 1 H), 8.81 (d, J=6Hz, 1H), 8.10 (d, J=9Hz, 1 H), 7.87 (t, J=6Hz, 1 H), 7.63-7.31 (m, 8H), 7.12 (d, J=9Hz, 1 H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CD<sub>2</sub>Cl<sub>2</sub>)□ δ (ppm): 115.5, 116.1, 122.3, 125.9, 127.2, 127.4, 129.0, 129.3, 134.0, 135.5, 137.3, 141.1, 150.4, 152.8, 154.8, 158.5.</p>
<heading id="h0020"><b><u>Synthesis of ligand 2-[(2-pyridyl)-methylimino]-4-chloro-phenol (L7).</u></b></heading>
<p id="p0062" num="0062">Ligand L7 was prepared following the same procedure as that used to prepare ligand L1 except that 740 mg (5 mmol) of 2-amino-4-chloro-phénol were used as reagent 2. 1203 mg of ligand L7 were obtained as brown solid with a yield of 99 %.
<chemistry id="chem0027" num="0027"><img id="ib0027" file="imgb0027.tif" wi="36" he="34" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="19"> -->
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.79 (s, 1H), 8.74 (d, J=6Hz, 1H), 8.18 (d, J=9Hz, 1H), 7.83 (t, J=6Hz, 1H), 7.43 (m, 1H), 7.38 (d, J=6Hz, 1H), 7.21 (dd, J=2Hz, J=9Hz, 1 H), 6.98 (d, J=9Hz, 1 H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CDCl<sub>3</sub>)□ δ (ppm): 116.3; 116.4; 121.8; 125.1; 125.5; 129.4; 135.1; 136.6; 149.8; 151.1; 153.7; 158.3.</p>
<heading id="h0021"><b><u>Synthesis of ligand 2-[(2-pyridyl)-methylimino]-4-nitro-phenol (L8)</u><sub><u>.</u></sub></b></heading>
<p id="p0063" num="0063">Ligand L8 was prepared following the same procedure as that used to prepare ligand L1 except that 803 mg (5 mmol) of 2-amino-4-nitro-phénol were used as reagent 2. 1029 mg of ligand L8 were obtained as beige solid with a yield of 85 %.
<chemistry id="chem0028" num="0028"><img id="ib0028" file="imgb0028.tif" wi="39" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 8.93 (s, 1H), 8.73 (d, J=6Hz, 1 H), 8.34 (d, J=6Hz, 1 H), 8.21 (d, J=9Hz, 1 H), 8.14 (dd, J=9Hz, 1H), 7.86 (t, J=9Hz, 1 H), 7.44 (m, 1H), 7.09 (d, J=9Hz, 1 H).</p>
<heading id="h0022"><b><u>Synthesis of ligand 2-[(2-(6-phenyl)-pyridyl)-methylimino]-phenol (L9).</u></b></heading>
<p id="p0064" num="0064">Ligand L9 was prepared following the same procedure as that used to prepare ligand L1 except that 184 mg (1 mmol) of precursor A were used as reagent 1. 261 mg of ligand L9 were obtained as yellow solid with a yield of 95 %.
<chemistry id="chem0029" num="0029"><img id="ib0029" file="imgb0029.tif" wi="43" he="34" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="20"> --></p>
<heading id="h0023"><b><u>Synthesis of ligand 2-[(2-(6-(2,6-dimethylphenyl)-pyridyl)-methylimino]-phenol (L10).</u></b></heading>
<p id="p0065" num="0065">Ligand L10 was prepared following the same procedure as that used to prepare ligand L1 except that 99 mg (1 mmol) of precursor C were used as reagent 1. 261 mg of ligand L10 were obtained as yellow solid with a yield of 95 %.
<chemistry id="chem0030" num="0030"><img id="ib0030" file="imgb0030.tif" wi="43" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<heading id="h0024"><b><u>Synthesis of ligand 2-[(2-(6-naphtyl)-pyridyl)methylimino]-phenol (L11).</u></b></heading>
<p id="p0066" num="0066">Ligand L11 was prepared following the same procedure as that used to prepare ligand L1 except that 233 mg (1 mmol) of precursor D were used as reagent 1. 149 mg of ligand L11 were obtained as yellow solid with a yield of 46 %.
<chemistry id="chem0031" num="0031"><img id="ib0031" file="imgb0031.tif" wi="48" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 8.92 (s,1H), 8.28 (d, J=6Hz, 1H), 8.10 (d, J=6Hz, 1H), 7.96 (m, 3H), 7.68-7.41 (m, 7H), 7.23 (t, J=6Hz, 1H), 7.01 (d, J=6Hz, 1 H), 6.88 (t, J=6Hz, 1 H)<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, CD<sub>2</sub>Cl<sub>2</sub>)□ δ (ppm): 115.7, 116.9, 120.2, 120.8, 125.9, 126.1, 126.5, 127.0, 127.2, 128.1, 128.9, 129.6, 130.4, 134.5, 137.7, 154.7, 158.6.</p>
<heading id="h0025"><b><u>Synthesis of ligand 2-[6-(2-phenyl)phenyl-2-pyridyl)-methylimino]-phenol (L12)</u>.</b></heading><!-- EPO <DP n="21"> -->
<p id="p0067" num="0067">Ligand L12 was prepared following the same procedure as that used to prepare ligand L1 except that 259 mg (1 mmol) of precursor B were used as reagent 1. 266 mg of ligand L12 were obtained as yellow solid with a yield of 67 %.
<chemistry id="chem0032" num="0032"><img id="ib0032" file="imgb0032.tif" wi="43" he="41" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm): 8.81 (s, 1H), 8.03(d, J=6Hz, 1H), 7.71-7.31 (m,7H), 7.21-6.92 (m, 8H).</p>
<heading id="h0026"><b><u>Synthesis of ligand 2-[(2-(6-phenyl)-pyridyl)-methylimino]-4-nitro-phenol (L13).</u></b></heading>
<p id="p0068" num="0068">Ligand L13 was prepared following the same procedure as that used to prepare ligand L1 except that 183 mg (1 mmol) of precursor A were used as reagent 1 and 154 mg (1 mmol) of 2-amino-4-nitrophénol as reagent 2. 240 mg of ligand L13 were obtained as yellow solid with a yield of 75 %.
<chemistry id="chem0033" num="0033"><img id="ib0033" file="imgb0033.tif" wi="53" he="35" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 9.02 (s,1H), 8.38 (d, J=3Hz, 1 H), 8.12 (d, J=9Hz, 2H), 8.08 (d, J=9Hz, 2H), 7.90 (m, 2H), 7.53-7.42 (m, 3H), 7.10 (d, J=9Hz, 1 H).</p>
<heading id="h0027"><b><u>Synthesis of ligand 2-[(2-(6-(2,6-dimethylphenyl)-pyridyl)-methylimino]-4-nitro-phenol (L14).</u></b></heading><!-- EPO <DP n="22"> -->
<p id="p0069" num="0069">Ligand L14 was prepared following the same procedure as that used to prepare ligand L1 except that 211 mg (1 mmol) of precursor C were used as reagent 1 and 154 mg (1 mmol) of 2-amino-4-nitrophénol as reagent 2. 108 mg of ligand L14 were obtained as yellow solid with a yield of 31 %.
<chemistry id="chem0034" num="0034"><img id="ib0034" file="imgb0034.tif" wi="53" he="36" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 8.92 (s,1H), 8.31 (d, J=3Hz, 1H), 8.12 (d, J=9Hz, 1H), 8.05-7.88 (m, 2H), 7.40 (d, J=9Hz, 1 H), 7.20 (t, J=9Hz, 1H), 7.10 (d, J=9Hz, 2H), 6.90 (d,J=9Hz, 1 H), 2.03 (s, 6H).</p>
<heading id="h0028"><b><u>Synthesis of ligand 2-[(2-(6-naphthyl)-pyridyl)-methylimino]-4-nitro-phenol (L15).</u></b></heading>
<p id="p0070" num="0070">Ligand L15 was prepared following the same procedure as that used to prepare ligand L1 except that 233 mg (1 mmol) of precursor D were used as reagent 1 and 154 mg (1 mmol) of 2-amino-4-nitrophénol as reagent 2. 320 mg of ligand L15 were obtained as yellow solid with a yield of 86 %.
<chemistry id="chem0035" num="0035"><img id="ib0035" file="imgb0035.tif" wi="57" he="36" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 9.02 (s,1H), 8.35 (d, J=3Hz, 1 H), 8.26 (d, J=9Hz, 1 H), 8.16-8.04 (m, 2H), 7.98 (t, J=9Hz, 1H), 7.96-7.92 (m, 2H), 7.72 (d, J=9Hz, 1 H), 7.63-7.48 (m, 4H), 7.09 (d, J=9Hz, 1 H), 2.03 (s, 6H).<!-- EPO <DP n="23"> --></p>
<heading id="h0029"><b><u>Synthesis of ligand 2-[(2-(6-(2-phenyl)phenyl)-pyridyl)-methylimino]-4-nitro-phenol (L16).</u></b></heading>
<p id="p0071" num="0071">Ligand L16 was prepared following the same procedure as that used to prepare ligand L1 except that 259 mg (1 mmol) of precursor B were used as reagent 1 and 154 mg (1 mmol) of 2-amino-4-nitrophénol as reagent 2. 390 mg of ligand L16 were obtained as yellow solid with a yield of 98 %.
<chemistry id="chem0036" num="0036"><img id="ib0036" file="imgb0036.tif" wi="52" he="43" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 8.90 (s,1H), 8.32 (s, 1H), 8.14 (m, 1 H), 8.01 (d, J=9Hz, 1 H), 7.73 (m, 1 H), 7.55-7.46 (m, 5H), 7.24-7.04 (m, 6H).</p>
<heading id="h0030"><b><u>Synthesis of ligand 2-[2-(6-methylpyridyl)-methylimino]-phenol (L17).</u></b></heading>
<p id="p0072" num="0072">Ligand L17 was prepared following the same procedure as that used to prepare ligand L1 except that 247 mg (1 mmol) of 2 picoline-6-carboxaldehyde were used as reagent 1 and 220 mg (2 mmol) of 2-aminophenol as reagent 2. 328 mg of ligand L17 were obtained as yellow solid with a yield of 77 %.
<chemistry id="chem0037" num="0037"><img id="ib0037" file="imgb0037.tif" wi="34" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm) : 2.63 (s, 3H), 6.75 (s, 1H), 6.95 (dt, J=2Hz and J=0.5Hz, 1H), 7.02 (dd, J=2Hz and J=0.3Hz, 1H), 7.26 (dt, J=2Hz and J=0.5Hz, 1 H), 7.30 (d, J=2Hz, 1H), 7.43 (dd, J=2Hz and 0.4Hz, 1H), 7.77 (t, J=2Hz,1 H), 8.01 (d, J=2Hz, 1 H), 8.82 (s, 1 H).<!-- EPO <DP n="24"> --></p>
<heading id="h0031"><u>Synthesis of ligand 2-[2-(6-methylpyridyl)-methylimino]-4-nitro-phenol (L18)</u></heading>
<p id="p0073" num="0073">Ligand L18 was prepared following the same procedure as that used to prepare ligand L1 except that 247 mg (1 mmol) of picoline-6-carboxaldehyde were used as reagent 1 and 321 mg (2 mmol) of 2-amino-4-phenol as reagent 2. 235 mg of ligand L18 were obtained as beige solid with a yield of 46 %.
<chemistry id="chem0038" num="0038"><img id="ib0038" file="imgb0038.tif" wi="44" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) : 2.55 (s, 3H), 7.09 (d, J=2.4Hz, 1H), 7.41 (d, J=1.9Hz, 1 H), 7.86 (t, J=2Hz, 1 H), 8.05 (m, 3H), 8.68 (s, 1 H), 11.0 (s, 1 H).</p>
<heading id="h0032"><b><u>Synthesis of ligand 2-[2-(6-methoxypyridyl)-methylimino]-4-nitro-phenol (L19)</u>.</b></heading>
<p id="p0074" num="0074">Ligand L19 was prepared following the same procedure as that used to prepare ligand L1 except that 640 mg (1 mmol) of precursor E were used as reagent 1 and 482 mg (3 mmol) of 2-amino-4-nitrophenol as reagent 2. 747 mg of ligand L18 were obtained as orange brown solid with a yield of 71 %.
<chemistry id="chem0039" num="0039"><img id="ib0039" file="imgb0039.tif" wi="53" he="35" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm): 3.91 (s,3H), 7.10 (q, J=2.3Hz, 3H), 7.44 (m, 2H), 7.86 (dd, J=0.4Hz and J=2.0Hz, 1H), 7.93 (d, J=1.9Hz, 1 H), 8.02 (d,<!-- EPO <DP n="25"> --> J=1.9Hz, 1H), 8.12 (d, J=1.9Hz, 1H), 8.25 (dd, J=0.6Hz and J=2.0Hz, 1H), 8.40 (d, J=0.6Hz, 1 H), 9.03 (s, 1 H).</p>
<heading id="h0033"><u>Synthesis of ligands 2-[2-(6-bromopyridyl)-methylimino]-4-nitro-phenol (L20)</u></heading>
<p id="p0075" num="0075">Ligand L20 was prepared following the same procedure as that used to prepare ligand L1 except that 767 mg (4 mmol) of 6-bromo-2-pyridine carboxaldehyde were used as reagent 1 and 642 mg (4 mmol) of 2-amino-4-phenol as reagent 2. 1.20 g of ligand L20 were obtained as beige solid with a yield of 92 %.
<chemistry id="chem0040" num="0040"><img id="ib0040" file="imgb0040.tif" wi="47" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) : 7.12 (d, J=2.2Hz, 1H), 7.83 (d, J=2.0Hz, 1H), 7.98 (t, J=1.9Hz, 1H), 8.08 (dd, J=2.2Hz and J=0.7Hz, 1H), 8.15 (d, J=0.7Hz, 1 H), 8.36 (d, J=1.9Hz, 1 H), 8.75 (s, 1 H), 11.0 (s, 1H).<br/>
<sup>13</sup>C{<sup>1</sup>H} NMR (75 MHz, DMSO)□ δ (ppm): 115.7, 116.0, 120.9, 120.8, 123.4, 129.6, 136.7, 139.4, 139.7, 140.5, 154.5, 157.0, 160.6.</p>
<heading id="h0034"><b><u>Synthesis of ligand 2-[2-(6-(quinolin-8-yl)-pyridyl)-methylimino]-phenol</u> (L21).</b></heading>
<p id="p0076" num="0076">Ligand L21 was prepared following the same procedure as that used to prepare ligand L1 except that 469 mg (2 mmol) of precursor F were used as reagent 1 and 220 mg (2 mmol) of 2-aminophenol as reagent 2. 389 mg of ligand L21 were obtained as beige solid with a yield of 60 %.<!-- EPO <DP n="26"> -->
<chemistry id="chem0041" num="0041"><img id="ib0041" file="imgb0041.tif" wi="44" he="35" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) : 6.95 (d, J=2.1Hz, 1 H), 7.10 (dd, J=2.0Hz and 0.5Hz, 1 H), 7.38 (d, J=0.5Hz, 1 H), 7.61 (q, J=1.0Hz, 1 H), 7.77 (t, J=2.0Hz, 1H), 8.06 (m, 2H), 8.20 (t, J=3.3Hz, 2H), 8.39 (d, J=3.3Hz, 1H), 8.45 (d, J=3.3Hz, 1 H), 8.80 (s, 1 H), 8.97 (d, J=0.7Hz, 1 H), 9.58 (s, 1H).</p>
<heading id="h0035"><b><u>Synthesis of ligand 2-[2-(6-(quinolin-8-yl)-pyridyl)-methylimino]-4-nitro-phenol (L22).</u></b></heading>
<p id="p0077" num="0077">Ligand L22 was prepared following the same procedure as that used to prepare ligand L1 except that 469 mg (2 mmol) of precursor F were used as reagent 1 and 321 mg (2 mmol) of 2-amino-4-nitrophenol as reagent 2. 538 mg of ligand L22 were obtained as beige solid with a yield of 73 %.
<chemistry id="chem0042" num="0042"><img id="ib0042" file="imgb0042.tif" wi="54" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) : 6.75 (d, J=2.1Hz, 1H), 7.38 (dd, J=2.2Hz and 0.7Hz, 1H), 7.45 (d, J=0.7Hz, 1H), 7.62 (dd, J=1.0Hz and J=2.1Hz, 1H), 7.79 (t, J=2.0Hz, 1H), 7.97 (d, J=2.2Hz, 1H), 8.10 (m, 2H), 8.22 (dd, J=1.8Hz and J=0.3Hz, 1H), 8.41 (dd, J=1.7 and J=0.2Hz, 1H), 8.51 (dd, J=1.6Hz and J=0.4Hz, 1 H), 8.96 (dd, J=1.0Hz and J=0.4Hz, 1 H), 10.1 (s, 1 H).</p>
<heading id="h0036"><b><u>Synthesis of ligand 2-[2-(6-trifluoromethylpyridyl)-methylimino]-phenol (L23).</u></b></heading><!-- EPO <DP n="27"> -->
<p id="p0078" num="0078">Ligand L23 was prepared following the same procedure as that used to prepare ligand L1 except that 628 mg (2.5 mmol) of precursor G were used as reagent 1 and 276 mg (2.5 mmol) of 2-aminophenol as reagent 2. 612 mg of ligand L23 were obtained as brown solid with a yield of 72 %.
<chemistry id="chem0043" num="0043"><img id="ib0043" file="imgb0043.tif" wi="43" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<heading id="h0037"><b><u>Synthesis of ligand 2-[2-(6-trifluoromethylpyridyl)-methylimino]-4-nitro-phenol (L24).</u></b></heading>
<p id="p0079" num="0079">Ligand L24 was prepared following the same procedure as that used to prepare ligand L1 except that 628 mg (2.5 mmol) of precursor G were used as reagent 1 and 401 mg (2.5 mmol) of 2-amino-4-nitrophenol as reagent 2. 658 mg of ligand L24 were obtained as beige solid with a yield of 68 %.
<chemistry id="chem0044" num="0044"><img id="ib0044" file="imgb0044.tif" wi="53" he="35" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) :7.10 (d, J=2.2Hz, 1H), 7.67 (dt, J=1.9Hz and 3.4Hz, 3H), 7.79 (d, J=1.9Hz, 1H), 7.90 (d, J=2.0Hz, 1H), 8.08 (m, 3H), 8.37 (d, J=2.0Hz,1 H), 8.75 (s, 1H), 11.00 (s, 1 H).</p>
<heading id="h0038"><b><u>Synthesis of ligand 2-[2-(6-(4-dibenzofuran))-methylimino]-phenol (L25).</u></b></heading>
<p id="p0080" num="0080">Ligand L25 was prepared following the same procedure as that used to prepare ligand L1 except that 547 mg (2 mmol) of precursor H were used as reagent 1<!-- EPO <DP n="28"> --> and 220 mg (2 mmol) of 2-aminophenol as reagent 2. 597 mg of ligand L25 were obtained as pale orange solid with a yield of 82 %.
<chemistry id="chem0045" num="0045"><img id="ib0045" file="imgb0045.tif" wi="44" he="38" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm) :7.00 (t, J=1.8Hz, 1H), 7.05 (d, J=2.0Hz, 1 H), 7.30 (t, J=1.8Hz, 1 H), 7.45 (t, J=1.8Hz, 2H), 7.55 (q, J=1.9Hz, 3H), 7.71 (d, J=2.0Hz, 1H), 8.04 (m, 3H), 8.26 (d, J=1.9Hz, 1H), 8.47 (d, J=1.8Hz, 1H), 8.60 (d, J=2.0Hz, 1 H), 9.00 (s, 1 H).</p>
<heading id="h0039"><b><u>Synthesis of ligand 2-[2-(6-(4-dibenzofuran))-methylimino]-4-nitrophenol (L26).</u></b></heading>
<p id="p0081" num="0081">Ligand L26 was prepared following the same procedure as that used to prepare ligand L1 except that 547 mg (2 mmol) of precursor H were used as reagent 1 and 321 mg (2 mmol) of 2-amino-4-nitrophenol as reagent 2. 603 mg of ligand L26 were obtained as beige orange solid with a yield of 74 %.
<chemistry id="chem0046" num="0046"><img id="ib0046" file="imgb0046.tif" wi="54" he="38" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, DMSO) δ (ppm) :6.76 (d, J=2.3Hz, 1H), 7.47 (t, J=1.9Hz, 1 H), 7.59 (dt, J=1.7Hz, 2H), 7.83 (d, J=2.0Hz, 1H), 7.98 (dd, J=1.9Hz, 1 H), 8.16 (m, 5H), 8.40 (t, J=1.7Hz, 2H), 8.58 (d, J=2.0Hz, 1H), 8.90 (s, 1H).<!-- EPO <DP n="29"> --></p>
<heading id="h0040"><b><u>Synthesis of ligand 2-[(2-pyridyl)-ethylimino]-phenol (L27).</u></b></heading>
<p id="p0082" num="0082">450 µl (3 mmol) of 2-acetylpyridine (reagent 1), 331 mg (3 mmol) of 2-aminophenol (reagent 2) and a few mg of para toluene sulfonic acid were dissolved in 20 mL of dry toluene. The reaction mixture was stirred at a temperature of 140°C for a period of time of 3 days. The solution was evaporated to dryness. After a chromatography on silica gel (heptane/AcOEt 8:2), 208 mg of ligand L27 were obtained as yellow solid with a yield of 33%.
<chemistry id="chem0047" num="0047"><img id="ib0047" file="imgb0047.tif" wi="30" he="34" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm) :2.43 (s, 3H), 6.66 (t, J=1.9Hz, 1H), 6.83 (dd, J=2.5Hz and J=1.7Hz, 1H), 7.06 (m, 1 H), 7.22 (s, 1H), 7.45 (dt, J=2.3Hz, 1 H), 7.69 (m, 2H), 8.61 (dt, J=1.1Hz, 1H), 10.01 (dt, J=1.8Hz, 1 H).</p>
<heading id="h0041"><b><u>Synthesis of ligand 2-[(2-pyridyl)-ethylimino]-4-nitrophenol (L28)</u><sub><u>.</u></sub></b></heading>
<p id="p0083" num="0083">Ligand L28 was prepared following the same procedure as that used to prepare ligand L27 except that 300µL (2 mmol) of 2-acetylpyridine were used as reagent 1 and 321 mg (2 mmol) of 2-amino-4-nitrophenol as reagent 2. 156 mg of ligand L28 were obtained as dark yellow solid with a yield of 30 %.
<chemistry id="chem0048" num="0048"><img id="ib0048" file="imgb0048.tif" wi="39" he="35" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="30"> -->
<sup>1</sup>H NMR (300 MHz, CD<sub>2</sub>Cl<sub>2</sub>) δ (ppm) : 2.42 (s, 3H), 6.66 (t, J=1.7Hz, 1H), 6.82 (t, J=2.0Hz, 1 H), 7.05 (m, 1H), 7.21 (s, 1 H), 7.43 (dd, J=2.3Hz, 1H), 7.67 (m, 2H), 8.60 (dd, J=1.2Hz, 1 H), 10.00 (dd, J=1.9Hz, 1H).</p>
<heading id="h0042"><b><u>Synthesis of ligand 2-[(2-pyridyl)-ethylimino]-1-propanol (L29).</u></b></heading>
<p id="p0084" num="0084">561 µl (5 mmol) of 2-pyridinecarboxaldehyde (reagent 1) and 376 mg (5 mmol) of 3-amino-1-propanol (reagent 2) were dissolved in 10 mL of dry ethanol and the reaction mixture was stirred during 24h. The solution was evaporated to dryness and the resulting oil was washed with pentane. Ligand L29 was obtained as yellow oil with a yield of 99%.
<chemistry id="chem0049" num="0049"><img id="ib0049" file="imgb0049.tif" wi="20" he="36" img-content="chem" img-format="tif"/></chemistry>
<sup>1</sup>H NMR (300 MHz, CDCl<sub>3</sub>) δ (ppm) : 2.00 (q, J=1.5Hz, 2H), 2.37 (s, 3H), 3.69 (t, J=1.6Hz, 2H), 3.92 (t, J=1.3Hz, 2H), 7.28 (t, J=2.2, 1 H), 7.69 (t, J=1.9Hz, 1H), 7.93 (d, J=2.0, 1 H), 8.58 (d, J=1.0Hz, 1 H).</p>
<heading id="h0043"><b><u>III. Preparation of metallic complexes.</u></b></heading>
<heading id="h0044"><u>Synthesis of titanium (Ti(IV)) complexes.</u></heading>
<p id="p0085" num="0085">198 mg (1 mmol) of ligand L1 was dissolved in 5 mL of THF and cooled to a temperature of -78°C. 1 mmol of n-butyl lithium (1,6M in hexane) was added drop-wise. The orange solution was stirred for 2 hours at room temperature. 1 mL (1 mmol) of TiCl<sub>4</sub> (1M in toluene) was dissolved in 5 mL of THF and cooled to a temperature of -78°C. The solution of the anionic ligand was added drop-wise to the solution of TiCl<sub>4</sub>. The resulting solution was stirred overnight at room temperature. The mixture was evaporated to dryness and the complex was extracted with 10 mL of dry dichloromethane. The filtrate was evaporated and<!-- EPO <DP n="31"> --> the residue was washed with 3 mL of diethyl ether, with 10 mL of pentane, and with another 10 mL of pentane. The resulting solid was dried under vacuum to afford 266 mg of complex A1 as brown-red powder with a yield of 76%.
<chemistry id="chem0050" num="0050"><img id="ib0050" file="imgb0050.tif" wi="33" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0086" num="0086">Complexes A3, A4, A5, A6, A7, A8, A11, A12, A13, A14, A15, A16, A17, A18, A22, A23, A24, A25, A26, A27 and A29 were obtained from ligands L3, L4, L5, L6, L7, L8, L11, L12, L13, L14, L15, L16, L17, L18, L22, L23, L24, L25, L26, L27 and L29 following the same procedure as that used for obtaining complex A1 from ligand L1.</p>
<p id="p0087" num="0087">The yields are summarised in Table I.
<tables id="tabl0001" num="0001">
<table frame="all">
<title><b><u>TABLE I.</u></b></title>
<tgroup cols="4">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="29mm"/>
<colspec colnum="4" colname="col4" colwidth="18mm"/>
<thead>
<row>
<entry align="center" valign="top">Ligand</entry>
<entry align="center" valign="top">Complex</entry>
<entry align="center" valign="top">Color of complex</entry>
<entry align="center" valign="top">Yield (%)</entry></row></thead>
<tbody>
<row>
<entry align="center">L3</entry>
<entry align="center">A3</entry>
<entry align="center">Dark red</entry>
<entry align="center">70</entry></row>
<row>
<entry align="center">L4</entry>
<entry align="center">A4</entry>
<entry align="center">brown</entry>
<entry align="center">60</entry></row>
<row>
<entry align="center">L5</entry>
<entry align="center">A5</entry>
<entry align="center">Dark red</entry>
<entry align="center">98</entry></row>
<row>
<entry align="center">L6</entry>
<entry align="center">A6</entry>
<entry align="center">Dark red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L7</entry>
<entry align="center">A7</entry>
<entry align="center">Dark red</entry>
<entry align="center">98</entry></row>
<row>
<entry align="center">L8</entry>
<entry align="center">A8</entry>
<entry align="center">Dark yellow</entry>
<entry align="center">76</entry></row>
<row>
<entry align="center">L11</entry>
<entry align="center">A11</entry>
<entry align="center">Dark red</entry>
<entry align="center">89</entry></row>
<row>
<entry align="center">L12</entry>
<entry align="center">A12</entry>
<entry align="center">Dark red</entry>
<entry align="center">67</entry></row>
<row>
<entry align="center">L13</entry>
<entry align="center">A13</entry>
<entry align="center">brown</entry>
<entry align="center">54</entry></row>
<row>
<entry align="center">L14</entry>
<entry align="center">A14</entry>
<entry align="center">brown</entry>
<entry align="center">61</entry></row><!-- EPO <DP n="32"> -->
<row>
<entry align="center">L15</entry>
<entry align="center">A15</entry>
<entry align="center">Dark yellow</entry>
<entry align="center">61</entry></row>
<row>
<entry align="center">L16</entry>
<entry align="center">A16</entry>
<entry align="center">beige</entry>
<entry align="center">82</entry></row>
<row>
<entry align="center">L17</entry>
<entry align="center">A17</entry>
<entry align="center">brown</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L18</entry>
<entry align="center">A18</entry>
<entry align="center">Dark red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L22</entry>
<entry align="center">A22</entry>
<entry align="center">Dark yellow</entry>
<entry align="center">13</entry></row>
<row>
<entry align="center">L23</entry>
<entry align="center">A23</entry>
<entry align="center">brown</entry>
<entry align="center">84</entry></row>
<row>
<entry align="center">L24</entry>
<entry align="center">A24</entry>
<entry align="center">brown</entry>
<entry align="center">72</entry></row>
<row>
<entry align="center">L25</entry>
<entry align="center">A25</entry>
<entry align="center">red</entry>
<entry align="center">70</entry></row>
<row>
<entry align="center">L26</entry>
<entry align="center">A26</entry>
<entry align="center">Dark red</entry>
<entry align="center">46</entry></row>
<row>
<entry align="center">L27</entry>
<entry align="center">A27</entry>
<entry align="center">red</entry>
<entry align="center">21</entry></row>
<row>
<entry align="center">L29</entry>
<entry align="center">A29</entry>
<entry align="center">yellow</entry>
<entry align="center">46</entry></row></tbody></tgroup>
</table>
</tables></p>
<heading id="h0045"><u>Synthesis of zirconium Zr(lV) complexes.</u></heading>
<p id="p0088" num="0088">0,8 mmol of ligand L1 was dissolved in 5 mL of THF and cooled to a temperature of -78°C. 0,8 mmol of n-butyl lithium (1.6 M in hexane) were added drop-wise. The solution was stirred for 30 minutes at room temperature. 0,8 mmol of ZrCl<sub>4</sub> were dissolved in 5 mL of THF and cooled to a temperature of -78°C. The solution of the anionic ligand was added drop-wise to the solution of ZrCl<sub>4</sub>. The resulting solution was stirred overnight under reflux at a temperature of 70°C. The mixture was concentrated to approximately 2 mL then 3mL of diethyl ether and 10 mL of pentane were added. Solvents were filtered off and the solid was washed twice with pentane. The resulting solid was dried under vacuum to afford 140 mg of complex B1 as orange powder with a yield of 47 %.
<chemistry id="chem0051" num="0051"><img id="ib0051" file="imgb0051.tif" wi="34" he="35" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="33"> --></p>
<p id="p0089" num="0089">Similarly, Zr(IV) complex B27 was obtained from ligand L27 as an orange powder with a yield of 77 %.
<chemistry id="chem0052" num="0052"><img id="ib0052" file="imgb0052.tif" wi="35" he="36" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0090" num="0090">Similarly, Zr(lV) complex B29 was obtained from ligand L29 as a yellow powder with a yield of 76 %.
<chemistry id="chem0053" num="0053"><img id="ib0053" file="imgb0053.tif" wi="24" he="36" img-content="chem" img-format="tif"/></chemistry></p>
<heading id="h0046"><u>Synthesis of Vanadium V(III) complexes.</u></heading>
<p id="p0091" num="0091">150 mg (0,8 mmol) of ligand L1 were dissolved in 5 mL of THF and cooled to a temperature of -78°C. 0,8 mmol of n-butyl lithium (1.6 M in hexane) were added drop-wise. The solution was stirred for 30 minutes at room temperature. 0,8 mmol of (THF)<sub>3</sub>VCl<sub>3</sub> were dissolved in 5 mL of THF and cooled to a temperature of -78°C. The solution of the anionic ligand was added drop-wise to the solution of VCl<sub>3</sub>. The resulting solution was stirred overnight at room temperature. The mixture was evaporated to dryness and the complex was extracted with 10 mL of dry dichloromethane. The filtrate was concentrated to approximately 2 mL, and 10 mL of pentane were added. Solvents were filtered off and the solid was washed twice with pentane. The resulting solid was dried under vacuum to afford 233 mg of complex C1 as brown powder with a yield of 97 %.<!-- EPO <DP n="34"> -->
<chemistry id="chem0054" num="0054"><img id="ib0054" file="imgb0054.tif" wi="33" he="36" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0092" num="0092">Similarly, V(III) complex C27 was obtained from ligand L27 as a dark orange powder with a yield of 62 %.
<chemistry id="chem0055" num="0055"><img id="ib0055" file="imgb0055.tif" wi="34" he="34" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0093" num="0093">Similarly, V(III) complex C29 was obtained from ligand L29 as a dark red powder with a yield of 99 %.
<chemistry id="chem0056" num="0056"><img id="ib0056" file="imgb0056.tif" wi="23" he="36" img-content="chem" img-format="tif"/></chemistry></p>
<heading id="h0047"><u>Synthesis of chromium Cr(III) complexes.</u></heading>
<p id="p0094" num="0094">100 mg (0.26 mmol) of ligand L1 was dissolved in 5 mL of THF and cooled to a temperature of -15°C. 1 mmol of n-butyl lithium (1,6M in hexane) was added drop-wise. The solution was stirred for 30 minutes and added to a solution of 101 mg (0.26 mmol) of (THF)<sub>3</sub>CrCl<sub>3</sub> dissolved in 5 mL of THF. The resulting solution was stirred overnight at room temperature. The mixture was concentrated to approximately 2 mL and 10 mL of pentane were added. Solvents were filtered off and the solid was washed twice with pentane. The<!-- EPO <DP n="35"> --> resulting solid was dried under vacuum to afford complex D1 as a red powder with a yield of 93 %.
<chemistry id="chem0057" num="0057"><img id="ib0057" file="imgb0057.tif" wi="35" he="35" img-content="chem" img-format="tif"/></chemistry></p>
<p id="p0095" num="0095">Complexes D3, D4, D5, D6, D7, D8, D21, D22, D23, D24, D25, D26, D27 and D29 were obtained from ligands L3, L4, L5, L6, L7, L8, L21, L22, L23, L24, L25, L26, L27 and L29 following the same procedure as that used for obtaining complex D1 from ligand L1.</p>
<p id="p0096" num="0096">The yields are summarised in Table II.<!-- EPO <DP n="36"> -->
<tables id="tabl0002" num="0002">
<table frame="all">
<title><b><u>TABLE II.</u></b></title>
<tgroup cols="4">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="29mm"/>
<colspec colnum="4" colname="col4" colwidth="18mm"/>
<thead>
<row>
<entry align="center" valign="top">Ligand</entry>
<entry align="center" valign="top">Complex</entry>
<entry align="center" valign="top">Color of complex</entry>
<entry align="center" valign="top">Yield (%)</entry></row></thead>
<tbody>
<row>
<entry align="center">L3</entry>
<entry align="center">D3</entry>
<entry align="center">dark red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L4</entry>
<entry align="center">D4</entry>
<entry align="center">red</entry>
<entry align="center">89</entry></row>
<row>
<entry align="center">L5</entry>
<entry align="center">D5</entry>
<entry align="center">Dark red</entry>
<entry align="center">66</entry></row>
<row>
<entry align="center">L6</entry>
<entry align="center">D6</entry>
<entry align="center">purple</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L7</entry>
<entry align="center">D7</entry>
<entry align="center">red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L8</entry>
<entry align="center">D8</entry>
<entry align="center">brown</entry>
<entry align="center">93</entry></row>
<row>
<entry align="center">L21</entry>
<entry align="center">D21</entry>
<entry align="center">black</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L22</entry>
<entry align="center">D22</entry>
<entry align="center">red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L23</entry>
<entry align="center">D23</entry>
<entry align="center">Dark red</entry>
<entry align="center">75</entry></row>
<row>
<entry align="center">L24</entry>
<entry align="center">D24</entry>
<entry align="center">brown</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L25</entry>
<entry align="center">D25</entry>
<entry align="center">red</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L26</entry>
<entry align="center">D26</entry>
<entry align="center">brown</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L27</entry>
<entry align="center">D27</entry>
<entry align="center">Dark yellow</entry>
<entry align="center">99</entry></row>
<row>
<entry align="center">L29</entry>
<entry align="center">D29</entry>
<entry align="center">Green</entry>
<entry align="center">99</entry></row></tbody></tgroup>
</table>
</tables></p>
<heading id="h0048"><u>Synthesis of fer Fe(III) complexes.</u></heading>
<p id="p0097" num="0097">150 mg (0.8 mmol) of ligand L1 were dissolved in 5 mL of THF and cooled to a temperature of -15°C. 0.8 mmol of n-butyl lithium (C=1,6M in hexane) were added dropwise. The solution was stirred for 30 minutes and added to a solution of 127 mg (0.8 mmol) of anhydrous FeCl<sub>3</sub> dissolved in 5 mL of THF. The solution was stirred at room temperature overnight. The mixture was concentrated to approximately 2 mL and then 10 mL of pentane were added. Solvents were filtered off and the solid was washed twice with pentane. The resulting solid was dried under vacuum to afford complex E1 as black powder with a yield of 92%.<!-- EPO <DP n="37"> -->
<chemistry id="chem0058" num="0058"><img id="ib0058" file="imgb0058.tif" wi="33" he="35" img-content="chem" img-format="tif"/></chemistry></p>
<heading id="h0049"><b><u>IV. Polymerisation of ethylene.</u></b></heading>
<heading id="h0050"><u>a. With methylaluminoxane (MAO) as activating agent.</u></heading>
<p id="p0098" num="0098">Ethylene polymerisation reactions were performed in a 20 mL stainless steel autoclave containing a glass insert, fitted with mechanical stirring, external thermocouple and pressure gauge and controlled by a computer. In a typical reaction run, the temperature was set at 50°C or 80°C and 4 mL of dry solvent (toluene or n-heptane) were introduced into the reactor under nitrogen flow. In an argon-filled glove box, about 4 mg (5 µmol) of the appropriate catalyst were weighted, activated with methylaluminoxane (MAO) activator (30 % wt in toluene) in an appropriate amount to obtain a ratio [Al]:[M] of 2000 and diluted with toluene to obtain a final volume of 2 mL. 200 µL of the solution of activated catalyst were placed inside the reactor. The injection loop was rinsed with 800 µL of solvent. The ethylene pressure was raised to 15 bars and ethylene was fed continuously into the reactor. After 1 hour or an ethylene consumption of 12 mmol, the reactor was cooled down and depressurised, then the reaction was quenched with isopropanol and the solution analysed by gas chromatography. The gas chromatographic (GC) analysis of the reaction products was performed on a Trace GC apparatus with a Petrocol capillary column (methyl silicone, 100 m long, i.d. 0.25 mm and film thickness of 0.5 µm) working at a temperature of 35°C for 15 min and then heating at a rate of 5° per minute up to a temperature of 250°C. The polymerisation results are displayed in Tables III for titanium complex and in Table IV for chromium complexes. GPC measurement could not be performed on all polymers because most polymers were not fully soluble in hot trichlorobenzene (140 to 180 °C) that was used as solvent.<!-- EPO <DP n="38"> -->
<tables id="tabl0003" num="0003">
<table frame="all">
<title><b><u>TABLE III.</u></b></title>
<tgroup cols="8">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="19mm"/>
<colspec colnum="4" colname="col4" colwidth="14mm"/>
<colspec colnum="5" colname="col5" colwidth="20mm"/>
<colspec colnum="6" colname="col6" colwidth="29mm"/>
<colspec colnum="7" colname="col7" colwidth="16mm"/>
<colspec colnum="8" colname="col8" colwidth="14mm"/>
<thead>
<row>
<entry morerows="1" align="center" valign="middle">Run</entry>
<entry morerows="1" align="center" valign="middle">Complex</entry>
<entry morerows="1" align="center" valign="middle">solvent</entry>
<entry morerows="1" align="center" valign="middle">T(°C)</entry>
<entry morerows="1" align="center" valign="middle">mPE (mg)</entry>
<entry morerows="1" align="center" valign="middle">Activity (kg/mol/h)</entry>
<entry namest="col7" nameend="col8" align="center" valign="middle">DSC</entry></row>
<row>
<entry align="center" valign="middle">Tm (°C)</entry>
<entry align="center" valign="middle">(J.g<sup>-1</sup>)</entry></row></thead>
<tbody>
<row>
<entry align="center">1</entry>
<entry align="center">A1</entry>
<entry align="center">toluene</entry>
<entry align="center">80</entry>
<entry align="center">174</entry>
<entry align="center">341</entry>
<entry align="center">133</entry>
<entry align="center">146,8</entry></row>
<row>
<entry align="center">2</entry>
<entry align="center">A1</entry>
<entry align="center">n-heptane</entry>
<entry align="center">80</entry>
<entry align="center">644</entry>
<entry align="center">1247</entry>
<entry align="center">133</entry>
<entry align="center">104,2</entry></row>
<row>
<entry align="center">3</entry>
<entry align="center">A1</entry>
<entry align="center">toluene</entry>
<entry align="center">50</entry>
<entry align="center">166</entry>
<entry align="center">324</entry>
<entry align="center">136</entry>
<entry align="center">148,0</entry></row>
<row>
<entry align="center">4</entry>
<entry align="center">A1</entry>
<entry align="center">n-heptane</entry>
<entry align="center">50</entry>
<entry align="center">367</entry>
<entry align="center">719</entry>
<entry align="center">133</entry>
<entry align="center">98,6</entry></row>
<row>
<entry align="center"/>
<entry align="center">A29</entry>
<entry align="center">n-heptane</entry>
<entry align="center">80</entry>
<entry align="center">453</entry>
<entry align="center">910</entry>
<entry align="center">*</entry>
<entry align="center">*</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0099" num="0099">All reactions were performed with 0.5 µmol of catalyst dissolved in 5 mL of solvent and MAO was added to give a [Al]:[Ti] ratio of 2000. Activities are expressed in kg of polyethylene per mol Ti per hour.<br/>
The obtained polymers were insoluble in hot trichlorobenzene and could not be caracterised by GPC.
<tables id="tabl0004" num="0004">
<table frame="all">
<title><b><u>TABLE IV.</u></b></title>
<tgroup cols="6">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="20mm"/>
<colspec colnum="4" colname="col4" colwidth="29mm"/>
<colspec colnum="5" colname="col5" colwidth="16mm"/>
<colspec colnum="6" colname="col6" colwidth="18mm"/>
<thead>
<row>
<entry morerows="1" align="center">Run</entry>
<entry morerows="1" align="center">Complex</entry>
<entry morerows="1" align="center" valign="middle">m PE (mg)</entry>
<entry morerows="1" align="center" valign="middle">Activity (kg/mol/h)</entry>
<entry namest="col5" nameend="col6" align="center" valign="middle">DSC</entry></row>
<row>
<entry align="center" valign="middle">Tm (°C)</entry>
<entry align="center" valign="middle">ΔH (J.g<sup>-1</sup>)</entry></row></thead>
<tbody>
<row>
<entry align="center" valign="bottom">5</entry>
<entry align="center" valign="bottom">D1</entry>
<entry align="center" valign="bottom">135</entry>
<entry align="center" valign="bottom">271</entry>
<entry align="center" valign="bottom">129</entry>
<entry align="center" valign="bottom">195,2</entry></row>
<row>
<entry align="center" valign="bottom">6</entry>
<entry align="center" valign="bottom">D3</entry>
<entry align="center" valign="bottom">129</entry>
<entry align="center" valign="bottom">252</entry>
<entry align="center" valign="bottom">131</entry>
<entry align="center" valign="bottom">169,5</entry></row>
<row>
<entry align="center" valign="bottom">7</entry>
<entry align="center" valign="bottom">D4</entry>
<entry align="center" valign="bottom">54</entry>
<entry align="center" valign="bottom">104</entry>
<entry align="center" valign="bottom">130</entry>
<entry align="center" valign="bottom">205,3</entry></row>
<row>
<entry align="center" valign="bottom">8</entry>
<entry align="center" valign="bottom">D5</entry>
<entry align="center" valign="bottom">162</entry>
<entry align="center" valign="bottom">312</entry>
<entry align="center" valign="bottom">127</entry>
<entry align="center" valign="bottom">193,1</entry></row>
<row>
<entry align="center" valign="bottom">9</entry>
<entry align="center" valign="bottom">D6</entry>
<entry align="center" valign="bottom">117</entry>
<entry align="center" valign="bottom">227</entry>
<entry align="center" valign="bottom">128</entry>
<entry align="center" valign="bottom">209,2</entry></row>
<row>
<entry align="center" valign="bottom">10</entry>
<entry align="center" valign="bottom">D7</entry>
<entry align="center" valign="bottom">158</entry>
<entry align="center" valign="bottom">320</entry>
<entry align="center" valign="bottom">130</entry>
<entry align="center" valign="bottom">181,9</entry></row>
<row>
<entry align="center" valign="bottom">11</entry>
<entry align="center" valign="bottom">D8</entry>
<entry align="center" valign="bottom">139</entry>
<entry align="center" valign="bottom">281</entry>
<entry align="center" valign="bottom">131</entry>
<entry align="center" valign="bottom">175</entry></row>
<row>
<entry align="center" valign="bottom">12</entry>
<entry align="center" valign="bottom">D1</entry>
<entry align="center" valign="bottom">77</entry>
<entry align="center" valign="bottom">154</entry>
<entry align="center" valign="bottom">129</entry>
<entry align="center" valign="bottom">210,5</entry></row>
<row>
<entry align="center" valign="bottom">13</entry>
<entry align="center" valign="bottom">D3</entry>
<entry align="center" valign="bottom">119</entry>
<entry align="center" valign="bottom">235</entry>
<entry align="center" valign="bottom">130</entry>
<entry align="center" valign="bottom">156,9</entry></row>
<row>
<entry align="center" valign="bottom">14</entry>
<entry align="center" valign="bottom">D4</entry>
<entry align="center" valign="bottom">79</entry>
<entry align="center" valign="bottom">152</entry>
<entry align="center" valign="bottom">129</entry>
<entry align="center" valign="bottom">178,0</entry></row>
<row>
<entry align="center" valign="bottom">15</entry>
<entry align="center" valign="bottom">D5</entry>
<entry align="center" valign="bottom">80</entry>
<entry align="center" valign="bottom">152</entry>
<entry align="center" valign="bottom">128</entry>
<entry align="center" valign="bottom">217,4</entry></row>
<row>
<entry align="center" valign="bottom">16</entry>
<entry align="center" valign="bottom">D6</entry>
<entry align="center" valign="bottom">75</entry>
<entry align="center" valign="bottom">153</entry>
<entry align="center" valign="bottom">130</entry>
<entry align="center" valign="bottom">218,3</entry></row>
<row>
<entry align="center" valign="bottom">17</entry>
<entry align="center" valign="bottom">D7</entry>
<entry align="center" valign="bottom">76</entry>
<entry align="center" valign="bottom">154</entry>
<entry align="center" valign="bottom">131</entry>
<entry align="center" valign="bottom">183,2</entry></row>
<row>
<entry align="center" valign="bottom">18</entry>
<entry align="center" valign="bottom">D8</entry>
<entry align="center" valign="bottom">91</entry>
<entry align="center" valign="bottom">190</entry>
<entry align="center" valign="bottom">131</entry>
<entry align="center" valign="bottom">120,6</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0100" num="0100">All reactions were performed with 0.5 µmol of catalyst dissolved in 5 mL of solvent, and MAO was added to give a [Al]:[Cr] ratio of 2000. Runs 5 to 11 were performed in toluene and runs 12 to 18 were performed in n-heptane. Activities are expressed in kg of polyethylene per mol Cr per hour. <sup>13</sup>C NMR analysis showed no short branches.<!-- EPO <DP n="39"> --></p>
<p id="p0101" num="0101">The obtained polymers were insoluble in hot trichlorobenzene and could not be caracterised by GPC.</p>
<heading id="h0051"><u>b. With tetra-isobutyldialuminoxane (IBAO) as activating agent.</u></heading>
<p id="p0102" num="0102">The procedure was the same as that described above with MAO except that the catalyst was activated with an appropriate amount of tetra-isobutyldialuminoxane ((iBu)<sub>2</sub>-Al-O-Al-(iBu)<sub>2</sub>) (10% wt in toluene). The polymerisation results are displayed in Table V.
<tables id="tabl0005" num="0005">
<table frame="all">
<title><b><u>TABLE V.</u></b></title>
<tgroup cols="4">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="18mm"/>
<colspec colnum="3" colname="col3" colwidth="20mm"/>
<colspec colnum="4" colname="col4" colwidth="32mm"/>
<thead>
<row>
<entry align="center" valign="middle"><b>Run</b></entry>
<entry align="center" valign="middle"><b>Complex</b></entry>
<entry align="center" valign="middle"><b>m PE (mg)</b></entry>
<entry align="center" valign="middle"><b>Activity (kg/mol/h)</b></entry></row></thead>
<tbody>
<row>
<entry align="center" valign="bottom">19</entry>
<entry align="center" valign="bottom">D1</entry>
<entry align="center" valign="bottom">293</entry>
<entry align="center" valign="bottom">588</entry></row>
<row>
<entry align="center" valign="bottom">20</entry>
<entry align="center" valign="bottom">D3</entry>
<entry align="center" valign="bottom">380</entry>
<entry align="center" valign="bottom">728</entry></row>
<row>
<entry align="center" valign="bottom">21</entry>
<entry align="center" valign="bottom">D4</entry>
<entry align="center" valign="bottom">271</entry>
<entry align="center" valign="bottom">534</entry></row>
<row>
<entry align="center" valign="bottom">22</entry>
<entry align="center" valign="bottom">D5</entry>
<entry align="center" valign="bottom">309</entry>
<entry align="center" valign="bottom">631</entry></row>
<row>
<entry align="center" valign="bottom">23</entry>
<entry align="center" valign="bottom">D6</entry>
<entry align="center" valign="bottom">348</entry>
<entry align="center" valign="bottom">690</entry></row>
<row>
<entry align="center" valign="bottom">24</entry>
<entry align="center" valign="bottom">D7</entry>
<entry align="center" valign="bottom">335</entry>
<entry align="center" valign="bottom">701</entry></row>
<row>
<entry align="center" valign="bottom">25</entry>
<entry align="center" valign="bottom">D8</entry>
<entry align="center" valign="bottom">208</entry>
<entry align="center" valign="bottom">380</entry></row>
<row>
<entry align="center" valign="bottom">26</entry>
<entry align="center" valign="bottom">D1</entry>
<entry align="center" valign="bottom">299</entry>
<entry align="center" valign="bottom">600</entry></row>
<row>
<entry align="center" valign="bottom">27</entry>
<entry align="center" valign="bottom">D3</entry>
<entry align="center" valign="bottom">398</entry>
<entry align="center" valign="bottom">761</entry></row>
<row>
<entry align="center" valign="bottom">28</entry>
<entry align="center" valign="bottom">D4</entry>
<entry align="center" valign="bottom">267</entry>
<entry align="center" valign="bottom">526</entry></row>
<row>
<entry align="center" valign="bottom">29</entry>
<entry align="center" valign="bottom">D5</entry>
<entry align="center" valign="bottom">528</entry>
<entry align="center" valign="bottom">1075</entry></row>
<row>
<entry align="center" valign="bottom">30</entry>
<entry align="center" valign="bottom">D6</entry>
<entry align="center" valign="bottom">390</entry>
<entry align="center" valign="bottom">774</entry></row>
<row>
<entry align="center" valign="bottom">31</entry>
<entry align="center" valign="bottom">D7</entry>
<entry align="center" valign="bottom">612</entry>
<entry align="center" valign="bottom">1293</entry></row>
<row>
<entry align="center" valign="bottom">32</entry>
<entry align="center" valign="bottom">D8</entry>
<entry align="center" valign="bottom">269</entry>
<entry align="center" valign="bottom">492</entry></row></tbody></tgroup>
</table>
</tables><!-- EPO <DP n="40"> --></p>
<p id="p0103" num="0103">All reactions were performed with 0.5 µmol of catalyst dissolved in 5 mL of toluene, at a temperature of 50°C, under an ethylene pressure of 15 bars. The amount of activating agent IBAO was adjusted to yield a ratio [Al]:[Cr] of 500. Runs 19 to 25 were performed in toluene and runs 26 to 32 were carried out in n-heptane.<br/>
Activities are expressed in kg of polyethylene per mol of Cr per hour.</p>
<p id="p0104" num="0104">When the catalyst components of the present invention are activated with IBAO, they exhibit a better activity than when activated with MAO. Without wishing to be bound by a theory, it is believed that IBAO, having a well defined structure, has a better activating efficiency than MAO that comes in oligomeric with residual trimethyaluminium.</p>
<p id="p0105" num="0105">The obtained polymers were insoluble in hot trichlorobenzene and could not be caracterised by GPC.</p>
<heading id="h0052"><u>c. Polymerisation of ethylene with supported catalysts.</u></heading>
<p id="p0106" num="0106">Ethylene polymerisation reactions were carried out in a 130 ml stainless steel autoclave equipped with mechanical stirring and a stainless steel injection cylinder. In a typical reaction run, the reactor was first dried under nitrogen flow at 100°C during 10 min. Then it was cooled down to the reaction temperature (50°C, 85°C or 95 °C) and 35 ml of isobutane were introduced into the reactor with a syringe pump, followed by the comonomer if required. The pressure was adjusted to the desired value (14.8, 23.8, 29 or 33 bar) with ethylene. In an argon-filled glove box, TiBAl (10 % wt in hexane), the appropriate supported catalyst (2 or 4 % wt based on the total weight of the supported catalyst, on MAO impregnated silica) and n-hexane were placed into the injection cylinder. The valve was closed and the cylinder was connected to the reactor under nitrogen flow. The active catalyst mixture was then introduced into the reactor with 40 ml of isobutane. After 1 hour, the reactor was cooled down to room temperature and slowly depressurised, and the polymer was recovered. The<!-- EPO <DP n="41"> --> comonomer, when present was hexene. The polymerisation results are displayed in Table VI.<!-- EPO <DP n="42"> -->
<tables id="tabl0006" num="0006">
<table frame="all">
<title><b><u>TABLE VI.</u></b></title>
<tgroup cols="10">
<colspec colnum="1" colname="col1" colwidth="20mm"/>
<colspec colnum="2" colname="col2" colwidth="21mm"/>
<colspec colnum="3" colname="col3" colwidth="18mm"/>
<colspec colnum="4" colname="col4" colwidth="11mm"/>
<colspec colnum="5" colname="col5" colwidth="17mm"/>
<colspec colnum="6" colname="col6" colwidth="15mm"/>
<colspec colnum="7" colname="col7" colwidth="24mm"/>
<colspec colnum="8" colname="col8" colwidth="15mm"/>
<colspec colnum="9" colname="col9" colwidth="15mm"/>
<colspec colnum="10" colname="col10" colwidth="13mm"/>
<thead>
<row>
<entry valign="top"><b>Complex</b></entry>
<entry valign="top"><b>Supporte d catalyst (mg)</b></entry>
<entry valign="top"><b>Hexene (ml)</b></entry>
<entry valign="top"><b>m PE (g)</b></entry>
<entry valign="top"><b>Prod. (g/g.h)</b></entry>
<entry valign="top"><b>Tm DSC (°C)</b></entry>
<entry valign="top"><b>SCB <sup>13</sup>C NMR</b></entry>
<entry valign="top"><b>Mw<sup>f</sup> kDa</b></entry>
<entry valign="top"><b>Mn kDa</b></entry>
<entry valign="top"><b>PDI</b></entry></row></thead>
<tbody>
<row>
<entry>A1 (2 wt %)</entry>
<entry>123.4</entry>
<entry>/</entry>
<entry align="char" char=".">2.4</entry>
<entry>19.4</entry>
<entry>131.9</entry>
<entry>0</entry>
<entry>Ins.</entry>
<entry/>
<entry/></row>
<row>
<entry>A1 (2 wt %)</entry>
<entry>124.1</entry>
<entry>1.6</entry>
<entry align="char" char=".">1.3</entry>
<entry>10.5</entry>
<entry>123.5</entry>
<entry>0.5 mol % (1.5wt%C6 )</entry>
<entry>Ins.</entry>
<entry/>
<entry/></row>
<row>
<entry>A1 (2 wt %)</entry>
<entry>124.0</entry>
<entry>/</entry>
<entry align="char" char=".">4.1</entry>
<entry>33.3<sup>a</sup></entry>
<entry>133.7</entry>
<entry>&lt; 0.1%</entry>
<entry>Ins.</entry>
<entry/>
<entry/></row>
<row>
<entry>D7 (4 wt %</entry>
<entry>304.4</entry>
<entry>/</entry>
<entry align="char" char=".">1.6</entry>
<entry>5.3<sup>b</sup></entry>
<entry>/</entry>
<entry>&lt; 0.1%</entry>
<entry>Ins.</entry>
<entry/>
<entry/></row>
<row>
<entry>D7 (4 wt %)</entry>
<entry>304.8</entry>
<entry>1.6</entry>
<entry align="char" char=".">1.2</entry>
<entry>3.9</entry>
<entry>125.9</entry>
<entry>0.5 mol % (1.5wt%C6 )</entry>
<entry>234.7</entry>
<entry>7.78</entry>
<entry>30.2</entry></row>
<row>
<entry>B7 4wt%</entry>
<entry>300.9</entry>
<entry>/</entry>
<entry align="char" char=".">2.2</entry>
<entry>14.6<sup>c</sup></entry>
<entry>128.9</entry>
<entry>/</entry>
<entry>538.6</entry>
<entry>10.69</entry>
<entry>50.4</entry></row>
<row>
<entry>B1 4wt%</entry>
<entry>302.2</entry>
<entry>/</entry>
<entry align="char" char=".">3.0</entry>
<entry>19.9<sup>d</sup></entry>
<entry>/</entry>
<entry>/</entry>
<entry>/</entry>
<entry/>
<entry/></row>
<row>
<entry>B1 4wt%</entry>
<entry>300.8</entry>
<entry>/</entry>
<entry align="char" char=".">2.2</entry>
<entry>7.3<sup>e</sup></entry>
<entry>129.2</entry>
<entry>&lt;0.1 mol%</entry>
<entry>228.8</entry>
<entry>12.97</entry>
<entry>17.6</entry></row>
<row>
<entry>C1 2wt%</entry>
<entry>300.8</entry>
<entry>/</entry>
<entry align="char" char=".">1.2</entry>
<entry>3.9</entry>
<entry>/</entry>
<entry>/</entry>
<entry>/</entry>
<entry/>
<entry/></row>
<row>
<entry>C1 2wt%</entry>
<entry>301.1</entry>
<entry>/</entry>
<entry align="char" char=".">1.3</entry>
<entry>4.3</entry>
<entry>/</entry>
<entry>/</entry>
<entry>/</entry>
<entry/>
<entry/></row></tbody></tgroup>
<tgroup cols="10" rowsep="0">
<colspec colnum="1" colname="col1" colwidth="20mm"/>
<colspec colnum="2" colname="col2" colwidth="21mm"/>
<colspec colnum="3" colname="col3" colwidth="18mm"/>
<colspec colnum="4" colname="col4" colwidth="11mm"/>
<colspec colnum="5" colname="col5" colwidth="17mm"/>
<colspec colnum="6" colname="col6" colwidth="15mm"/>
<colspec colnum="7" colname="col7" colwidth="24mm"/>
<colspec colnum="8" colname="col8" colwidth="15mm"/>
<colspec colnum="9" colname="col9" colwidth="15mm"/>
<colspec colnum="10" colname="col10" colwidth="13mm"/>
<tbody>
<row>
<entry namest="col1" nameend="col10" align="justify">All reactions were performed in isobutane, at a polymerisation temperature of 85°C, under an ethylene pressure of 23.8 bars, with 25.6 mg of TiBAl as cocatalyst. Polymerisations were stopped after a period of time of 1 hour.<br/>
<sup>a</sup> at 29 bar with 44.7 mg of tris-n-octyl-aluminium (TnOAI) instead of TIBAI.<br/>
<sup>b</sup> at 50°C under 14.8 bars of ethylene.<br/>
<sup>c</sup> at 29 bar with 156 mg of IBAO instead of TiBAI ; 30 min. instead of 1 h.<br/>
<sup>d</sup> at 95°C and 33 bar with 130 mg of IBAO instead of TiBAl ; 30 min. instead of 1 h.<br/>
<sup>e</sup> 130 mg of IBAO instead of TiBAl.<br/>
<sup>f</sup> Calculated for the curve between log(M) 3 to 8. For GPC curves, see <figref idref="f0001 f0002">figures 1 to 3</figref>.<br/>
Ins. means insoluble.</entry></row></tbody></tgroup>
</table>
</tables><!-- EPO <DP n="43"> --></p>
<heading id="h0053"><u>d. Polymerisation of ethylene in the presence of hydrogen as a chain transfer agent.</u></heading>
<p id="p0107" num="0107">The procedure was the same as that described above with MAO in paragraph IV.a except that the reactor was first pressurised with hydrogen, followed by ethylene to reach a final pressure of 19 bar. The polymerisation results are displayed in Table VII.
<tables id="tabl0007" num="0007">
<table frame="all">
<title><b><u>TABLE VII.</u></b></title>
<tgroup cols="10">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="20mm"/>
<colspec colnum="3" colname="col3" colwidth="18mm"/>
<colspec colnum="4" colname="col4" colwidth="19mm"/>
<colspec colnum="5" colname="col5" colwidth="22mm"/>
<colspec colnum="6" colname="col6" colwidth="13mm"/>
<colspec colnum="7" colname="col7" colwidth="16mm"/>
<colspec colnum="8" colname="col8" colwidth="18mm"/>
<colspec colnum="9" colname="col9" colwidth="15mm"/>
<colspec colnum="10" colname="col10" colwidth="14mm"/>
<thead>
<row>
<entry morerows="1" align="center" valign="middle">Run</entry>
<entry morerows="1" align="center" valign="middle">Complex</entry>
<entry morerows="1" align="center" valign="middle">[H<sub>2</sub>]:[Ti]</entry>
<entry morerows="1" align="center" valign="middle">m Polymer (mg)</entry>
<entry morerows="1" align="center" valign="middle">Activity (kg/mol/h)</entry>
<entry namest="col6" nameend="col7" align="center" valign="middle">DSC</entry>
<entry namest="col8" nameend="col10" align="center" valign="middle">GPC</entry></row>
<row>
<entry align="center" valign="middle">Tm (°C)</entry>
<entry align="center" valign="middle">ΔH (J.g<sup>-1</sup>)</entry>
<entry align="center" valign="middle">Mw</entry>
<entry align="center" valign="middle">Mn</entry>
<entry align="center" valign="middle">PDI</entry></row></thead>
<tbody>
<row>
<entry align="center" valign="middle">33</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry valign="middle" align="char" char="." charoff="10">0.06</entry>
<entry align="center" valign="middle">78</entry>
<entry align="center" valign="middle">152</entry>
<entry align="center" valign="middle">129</entry>
<entry valign="middle" align="char" char=".">160.4</entry>
<entry align="center" valign="middle">278100</entry>
<entry align="center" valign="middle">9430</entry>
<entry align="center" valign="middle">29.5</entry></row>
<row>
<entry align="center" valign="middle">34</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry valign="middle" align="char" char="." charoff="10">0.11</entry>
<entry align="center" valign="middle">61</entry>
<entry align="center" valign="middle">119</entry>
<entry align="center" valign="middle">128</entry>
<entry valign="middle" align="char" char=".">179.8</entry>
<entry align="center" valign="middle">201800</entry>
<entry align="center" valign="middle">7160</entry>
<entry align="center" valign="middle">28.2</entry></row>
<row>
<entry align="center" valign="middle">35</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry valign="middle" align="char" char="." charoff="10">0.17</entry>
<entry align="center" valign="middle">69</entry>
<entry align="center" valign="middle">135</entry>
<entry align="center" valign="middle">128</entry>
<entry valign="middle" align="char" char=".">173.7</entry>
<entry namest="col8" nameend="col10" align="center" valign="middle">insoluble</entry></row>
<row>
<entry align="center" valign="middle">36</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry valign="middle" align="char" char="." charoff="10">0.20</entry>
<entry align="center" valign="middle">60</entry>
<entry align="center" valign="middle">117</entry>
<entry align="center" valign="middle">128</entry>
<entry valign="middle" align="char" char=".">160.3</entry>
<entry align="center" valign="middle">218000</entry>
<entry align="center" valign="middle">8400</entry>
<entry align="center" valign="middle">26.0</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0108" num="0108">The reaction was performed with 0.5 µmol of catalyst dissolved in 5 mL of n-heptane, at a temperature 80°C under a hydrogen-ethylene pressure of 19 bars and with MAO as activating agent. The amount of activating agent MAO was adjusted to yield a ratio [Al]:[Ti] of 2000.</p>
<p id="p0109" num="0109">Activities are expressed in kg polyethylene per mol of Ti per hour. PDI is the polydispersity index defined as the ratio Mw/Mn of the weight average molecular weight Mw over the number average molecular weight Mn.</p>
<heading id="h0054"><u>e. Polymerisation of ethylene in the presence of diethyl zinc as a chain transfer agent.</u></heading>
<p id="p0110" num="0110">The procedure was the same as that described above with MAO in paragraph IV.a except that an appropriate amount of diethyl zinc (ZnEt<sub>2</sub>) was injected in the reactor before adding the catalyst. The polymerisation results are displayed in Table VIII.<!-- EPO <DP n="44"> -->
<tables id="tabl0008" num="0008">
<table frame="all">
<title><b><u>TABLE VIII.</u></b></title>
<tgroup cols="10">
<colspec colnum="1" colname="col1" colwidth="12mm"/>
<colspec colnum="2" colname="col2" colwidth="19mm"/>
<colspec colnum="3" colname="col3" colwidth="22mm"/>
<colspec colnum="4" colname="col4" colwidth="18mm"/>
<colspec colnum="5" colname="col5" colwidth="21mm"/>
<colspec colnum="6" colname="col6" colwidth="12mm"/>
<colspec colnum="7" colname="col7" colwidth="19mm"/>
<colspec colnum="8" colname="col8" colwidth="17mm"/>
<colspec colnum="9" colname="col9" colwidth="15mm"/>
<colspec colnum="10" colname="col10" colwidth="13mm"/>
<thead>
<row>
<entry morerows="1" align="center" valign="middle">Run</entry>
<entry morerows="1" align="center" valign="middle">Complex</entry>
<entry morerows="1" align="center" valign="middle">[ZnEt<sub>2</sub>]:[Ti]</entry>
<entry morerows="1" align="center" valign="middle">m Polymer (mg)</entry>
<entry morerows="1" align="center" valign="middle">Activity (kg/mol/h)</entry>
<entry namest="col6" nameend="col7" align="center" valign="middle">DSC</entry>
<entry namest="col8" nameend="col10" align="center" valign="middle">GPC</entry></row>
<row>
<entry align="center" valign="middle">Tm (°C)</entry>
<entry align="center" valign="middle">ΔH(J.g<sup>-1</sup>)</entry>
<entry align="center" valign="middle">Mw</entry>
<entry align="center" valign="middle">Mn</entry>
<entry align="center" valign="middle">PDI</entry></row></thead>
<tbody>
<row>
<entry align="center" valign="middle">37</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">100</entry>
<entry align="center" valign="middle">691</entry>
<entry align="center" valign="middle">1349</entry>
<entry align="center" valign="middle">135</entry>
<entry valign="middle" align="char" char="." charoff="28">177.2</entry>
<entry align="center" valign="middle">410450</entry>
<entry align="center" valign="middle">29220</entry>
<entry align="center" valign="middle">14.0</entry></row>
<row>
<entry align="center" valign="middle">38</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">250</entry>
<entry align="center" valign="middle">342</entry>
<entry align="center" valign="middle">668</entry>
<entry align="center" valign="middle">134</entry>
<entry valign="middle" align="char" char="." charoff="28">190.8</entry>
<entry align="center" valign="middle">155800</entry>
<entry align="center" valign="middle">15460</entry>
<entry align="center" valign="middle">10.1</entry></row>
<row>
<entry align="center" valign="middle">39</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">500</entry>
<entry align="center" valign="middle">317</entry>
<entry align="center" valign="middle">619</entry>
<entry align="center" valign="middle">132</entry>
<entry valign="middle" align="char" char="." charoff="28">216.3</entry>
<entry align="center" valign="middle">86450</entry>
<entry align="center" valign="middle">7190</entry>
<entry align="center" valign="middle">12.0</entry></row>
<row>
<entry align="center" valign="middle">40</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">1000</entry>
<entry align="center" valign="middle">226</entry>
<entry align="center" valign="middle">441</entry>
<entry align="center" valign="middle">129</entry>
<entry valign="middle" align="char" char="." charoff="28">224.6</entry>
<entry align="center" valign="middle">19410</entry>
<entry align="center" valign="middle">3840</entry>
<entry align="center" valign="middle">5.1</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0111" num="0111">The reaction was performed with 0.5 µmol of catalyst dissolved in 5 mL of n-heptane, at a temperature 80°C under an ethylene pressure of 19 bars and with MAO as activating agent. The amount of activating agent MAO was adjusted to yield a ratio [Al]:[Ti] of 2000.<br/>
Activities are expressed in kg polyethylene per mol of Ti per hour.<br/>
PDI is the polydispersity index defined as the ratio Mw/Mn of the weight average molecular weight Mw over the number average molecular weight Mn.</p>
<heading id="h0055"><u>f. Polymerisation of ethylene in the presence of methylaluminoxane (MAO) or tetra-isobutyldialuminoxane (IBAO) as activating agent.</u></heading>
<p id="p0112" num="0112">Ethylene polymerisation reactions were performed in a 24 parallel reactors unit containing glass inserts of 50 ml and magnetic stirrers. In a typical reaction run, the catalyst was introduced into the glass insert. Then the activator (MAO or IBAO) and the solvent (22 to 24 ml of heptane) were added. The glass insert was sealed with a septum and placed into the 24 parallel reactors unit. While closing the reactor, the septum was pierced by a needle. The stirring was set at 1000 rpm and the temperature was set at 80°C. Then the pressure was raised to 22 bar of ethylene. These conditions were maintained during 20 min. The polymerisation results are displayed in Tables IX and X.<!-- EPO <DP n="45"> -->
<tables id="tabl0009" num="0009">
<table frame="all">
<title><b><u>TABLE IX.</u></b></title>
<tgroup cols="10">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="14mm"/>
<colspec colnum="3" colname="col3" colwidth="14mm"/>
<colspec colnum="4" colname="col4" colwidth="14mm"/>
<colspec colnum="5" colname="col5" colwidth="14mm"/>
<colspec colnum="6" colname="col6" colwidth="21mm"/>
<colspec colnum="7" colname="col7" colwidth="17mm"/>
<colspec colnum="8" colname="col8" colwidth="16mm"/>
<colspec colnum="9" colname="col9" colwidth="14mm"/>
<colspec colnum="10" colname="col10" colwidth="16mm"/>
<thead>
<row>
<entry namest="col1" nameend="col2" align="center"><b>Complex</b></entry>
<entry namest="col3" nameend="col4" align="center"><b>Activator</b></entry>
<entry align="center"><b>PE</b></entry>
<entry align="center"><b>Activity</b></entry>
<entry namest="col7" nameend="col9" align="center"><b>HT-GPC</b></entry>
<entry><b>DSC</b></entry></row>
<row>
<entry align="center"/>
<entry align="center"><b>mg</b></entry>
<entry align="center"/>
<entry align="center"><b>ml</b></entry>
<entry align="center"><b>g</b></entry>
<entry align="center"><b>Kg/mmol.h</b></entry>
<entry align="center"><b>Mw (Da)</b></entry>
<entry align="center"><b>Mn (Da)</b></entry>
<entry align="center"><b>PDI</b></entry>
<entry><b>Tm (°C)</b></entry></row></thead>
<tbody>
<row>
<entry align="center" valign="middle">B27</entry>
<entry align="center" valign="middle">0.978</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">1.2</entry>
<entry align="center" valign="middle">0.92</entry>
<entry valign="middle" align="char" char="." charoff="9">1.17</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">B27</entry>
<entry align="center" valign="middle">0.98</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">1.2</entry>
<entry align="center" valign="middle">0.87</entry>
<entry valign="middle" align="char" char="." charoff="9">1.10</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">C27</entry>
<entry align="center" valign="middle">0.933</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">1.2</entry>
<entry align="center" valign="middle">0.51</entry>
<entry valign="middle" align="char" char="." charoff="9">0.55</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">C27</entry>
<entry align="center" valign="middle">1.367</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">1.2</entry>
<entry align="center" valign="middle">0.59</entry>
<entry valign="middle" align="char" char="." charoff="9">0.44</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A1</entry>
<entry align="center" valign="middle">0.57</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.6</entry>
<entry align="center" valign="middle">0.95</entry>
<entry valign="middle" align="char" char="." charoff="9">1.77</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A1</entry>
<entry align="center" valign="middle">0.57</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.6</entry>
<entry align="center" valign="middle">1.05</entry>
<entry valign="middle" align="char" char="." charoff="9">1.96</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A27</entry>
<entry align="center" valign="middle">0.53</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.6</entry>
<entry align="center" valign="middle">0.68</entry>
<entry valign="middle" align="char" char="." charoff="9">1.42</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A27</entry>
<entry align="center" valign="middle">0.53</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.6</entry>
<entry align="center" valign="middle">0.68</entry>
<entry valign="middle" align="char" char="." charoff="9">1.42</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">D27</entry>
<entry align="center" valign="middle">1.248</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.253</entry>
<entry valign="middle" align="char" char="." charoff="9">0.21</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">D27</entry>
<entry align="center" valign="middle">1.044</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.214</entry>
<entry valign="middle" align="char" char="." charoff="9">0.21</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">C27</entry>
<entry align="center" valign="middle">0.96</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.104</entry>
<entry valign="middle" align="char" char="." charoff="9">0.11</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">C27</entry>
<entry align="center" valign="middle">0.953</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.129</entry>
<entry valign="middle" align="char" char="." charoff="9">0.14</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A3</entry>
<entry align="center" valign="middle">0.54</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.163</entry>
<entry align="center" valign="middle">1.18</entry>
<entry valign="middle" align="char" char="." charoff="9">1.60</entry>
<entry align="center" valign="middle">insoluble</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle">135.4</entry></row>
<row>
<entry align="center" valign="middle">A3</entry>
<entry align="center" valign="middle">0.54</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.163</entry>
<entry align="center" valign="middle">1.17</entry>
<entry valign="middle" align="char" char="." charoff="9">1.58</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">A15</entry>
<entry align="center" valign="middle">0.522</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.163</entry>
<entry align="center" valign="middle">0.73</entry>
<entry valign="middle" align="char" char="." charoff="9">1.46</entry>
<entry align="center" valign="middle">insoluble</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle">137.1</entry></row>
<row>
<entry align="center" valign="middle">A15</entry>
<entry align="center" valign="middle">0.522</entry>
<entry align="center" valign="middle">MAO</entry>
<entry align="center" valign="middle">0.163</entry>
<entry align="center" valign="middle">0.68</entry>
<entry valign="middle" align="char" char="." charoff="9">1.36</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">D6</entry>
<entry align="center" valign="middle">1.66</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">1.05</entry>
<entry valign="middle" align="char" char="." charoff="9">0.76</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">D1</entry>
<entry align="center" valign="middle">1.44</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.70</entry>
<entry valign="middle" align="char" char="." charoff="9">0.47</entry>
<entry align="center" valign="middle">275543</entry>
<entry align="center" valign="middle">11545</entry>
<entry align="center" valign="middle">23.9</entry>
<entry align="center" valign="middle">130.9</entry></row>
<row>
<entry align="center" valign="middle">D1</entry>
<entry align="center" valign="middle">1.55</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.57</entry>
<entry valign="middle" align="char" char="." charoff="9">0.36</entry>
<entry align="center" valign="middle">187629</entry>
<entry align="center" valign="middle">8662</entry>
<entry align="center" valign="middle">21.7</entry>
<entry align="center" valign="middle">131.7</entry></row>
<row>
<entry align="center" valign="middle">D7</entry>
<entry align="center" valign="middle">1.57</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.66</entry>
<entry valign="middle" align="char" char="." charoff="9">0.45</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row>
<row>
<entry align="center" valign="middle">D7</entry>
<entry align="center" valign="middle">1.46</entry>
<entry align="center" valign="middle">IBAO</entry>
<entry align="center" valign="middle">2.6</entry>
<entry align="center" valign="middle">0.66</entry>
<entry valign="middle" align="char" char="." charoff="9">0.49</entry>
<entry align="center" valign="middle">/</entry>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/>
<entry align="center" valign="middle"/></row></tbody></tgroup>
</table>
</tables>
Conditions : Heptane 22-24 ml, 80°C, ethylene 22 bar, 20-30 min., 1000 rpm.<br/>
For GPC curves,see <figref idref="f0003">figure 4</figref>.
<tables id="tabl0010" num="0010">
<table frame="none">
<title><b><u>TABLE X.</u></b></title>
<tgroup cols="8" colsep="0" rowsep="0">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="14mm"/>
<colspec colnum="3" colname="col3" colwidth="14mm"/>
<colspec colnum="4" colname="col4" colwidth="14mm"/>
<colspec colnum="5" colname="col5" colwidth="14mm"/>
<colspec colnum="6" colname="col6" colwidth="32mm"/>
<colspec colnum="7" colname="col7" colwidth="17mm"/>
<colspec colnum="8" colname="col8" colwidth="25mm"/>
<thead>
<row>
<entry namest="col1" nameend="col2" align="center" valign="top"><b>Complex</b></entry>
<entry namest="col3" nameend="col4" align="center" valign="top"><b>Activator</b></entry>
<entry align="center" valign="top"><b>PE</b></entry>
<entry align="center" valign="top"><b>Activity Kg/mmol.</b></entry>
<entry align="center" valign="top"><b>HT-GPC</b></entry>
<entry align="center" valign="top"><b>DSC Tm(°C )</b></entry></row>
<row>
<entry align="center" valign="top"/>
<entry align="center" valign="top"><b>mg</b></entry>
<entry align="center" valign="top"/>
<entry align="center" valign="top"><b>ml</b></entry>
<entry align="center" valign="top"><b>g</b></entry>
<entry align="center" valign="top"><b>h</b></entry>
<entry valign="top"/>
<entry valign="top"/></row></thead>
<tbody>
<row>
<entry>D1</entry>
<entry align="char" char="." charoff="13">1.47</entry>
<entry>IBAO</entry>
<entry align="char" char="." charoff="13">2.6</entry>
<entry align="char" char="." charoff="13">0.19</entry>
<entry align="char" char="." charoff="6">0.13</entry>
<entry align="center">/</entry>
<entry align="center">/</entry></row>
<row>
<entry>D1</entry>
<entry align="char" char="." charoff="13">1.23</entry>
<entry>IBAO</entry>
<entry align="char" char="." charoff="13">2.5</entry>
<entry align="char" char="." charoff="13">0.18</entry>
<entry align="char" char="." charoff="6">0.14</entry>
<entry align="center">Insoluble</entry>
<entry align="center">134.1</entry></row>
<row>
<entry>D6</entry>
<entry align="char" char="." charoff="13">1.85</entry>
<entry>IBAO</entry>
<entry align="char" char="." charoff="13">2.6</entry>
<entry align="char" char="." charoff="13">0.11</entry>
<entry align="char" char="." charoff="6">0.07</entry>
<entry align="center">/</entry>
<entry align="center">/</entry></row></tbody></tgroup>
</table>
</tables><!-- EPO <DP n="46"> -->
Conditions : Heptane 22 ml, 50°C, ethylene 15 bar, 20-30 min., 1000 rpm.<!-- EPO <DP n="47"> --></p>
<heading id="h0056"><b>V. Copolymerisation reactions.</b></heading>
<heading id="h0057"><u>a. Copolymerisation of ethylene with propylene.</u></heading>
<p id="p0113" num="0113">The procedure was the same as that described above with MAO in paragraph IV.a except that the reaction was performed at 80°C, and that the reactor was first pressurised with propylene, followed by ethylene to a final pressure of 19 bar in order to obtain a mixture of 10% of propylene (molar fraction) in ethylene. The polymerisation results are displayed in Table XI.
<tables id="tabl0011" num="0011">
<table frame="all">
<title><b><u>TABLE XI.</u></b></title>
<tgroup cols="7">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="27mm"/>
<colspec colnum="4" colname="col4" colwidth="29mm"/>
<colspec colnum="5" colname="col5" colwidth="14mm"/>
<colspec colnum="6" colname="col6" colwidth="14mm"/>
<colspec colnum="7" colname="col7" colwidth="27mm"/>
<thead>
<row>
<entry morerows="1" align="center" valign="middle">Run</entry>
<entry morerows="1" align="center" valign="middle">Complex</entry>
<entry morerows="1" align="center" valign="middle">m Polymer (mg)</entry>
<entry morerows="1" align="center" valign="middle">Activity (kg/mol/h)</entry>
<entry namest="col5" nameend="col6" align="center" valign="middle">DSC</entry>
<entry morerows="1" align="center" valign="middle">% Me branching</entry></row>
<row>
<entry align="center" valign="middle">(°C)</entry>
<entry align="center" valign="middle">ΔH</entry></row></thead>
<tbody>
<row>
<entry align="center" valign="middle">41</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">293</entry>
<entry align="center" valign="middle">572</entry>
<entry align="center" valign="middle">126</entry>
<entry align="center" valign="middle">127.4</entry>
<entry align="center" valign="middle">2.2</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0114" num="0114">The reaction was performed with 0.5 µmol of catalyst dissolved in 5 mL of n-heptane, at a temperature 80°C under an ethylene pressure of 19 bars and with MAO as activating agent. The amount of activating agent MAO was adjusted to yield a ratio [Al]:[Ti] of 2000.<br/>
Activities are expressed in kg copolymer per mol of Ti per hour.</p>
<p id="p0115" num="0115">The obtained polymers were insoluble in hot trichlorobenzene and could not be caracterised by GPC.</p>
<heading id="h0058"><u>b. Copolymerisation of ethylene with vinyltrimethylsilane.</u></heading>
<p id="p0116" num="0116">The procedure was the same as that described above with MAO in paragraph IV.a except that an appropriate amount of vinyltrimethylsilane was injected in the reactor before adding the catalyst. The reaction was performed at 80°C and to pressure of 19 bar. The polymerisation results are displayed in Table XII.<!-- EPO <DP n="48"> -->
<tables id="tabl0012" num="0012">
<table frame="all">
<title><b><u>TABLE XII.</u></b></title>
<tgroup cols="5">
<colspec colnum="1" colname="col1" colwidth="14mm"/>
<colspec colnum="2" colname="col2" colwidth="17mm"/>
<colspec colnum="3" colname="col3" colwidth="21mm"/>
<colspec colnum="4" colname="col4" colwidth="27mm"/>
<colspec colnum="5" colname="col5" colwidth="29mm"/>
<thead>
<row>
<entry align="center" valign="middle">Run</entry>
<entry align="center" valign="middle">Complex</entry>
<entry align="center" valign="middle">[Silane]:[Ti]</entry>
<entry align="center" valign="middle">m Polymer (mg)</entry>
<entry align="center" valign="middle">Activity (kg/mol/h)</entry></row></thead>
<tbody>
<row>
<entry align="center" valign="middle">42</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">500:1.</entry>
<entry align="center" valign="middle">610</entry>
<entry align="center" valign="middle">1191</entry></row>
<row>
<entry align="center" valign="middle">43</entry>
<entry align="center" valign="middle"><b>A1</b></entry>
<entry align="center" valign="middle">2000:1</entry>
<entry align="center" valign="middle">740</entry>
<entry align="center" valign="middle">1147</entry></row></tbody></tgroup>
</table>
</tables></p>
<p id="p0117" num="0117">The reaction was performed with 0.5 µmol of catalyst dissolved in 5 mL of n-heptane, at a temperature 80°C under an ethylene pressure of 19 bars and with MAO as activating agent. The amount of activating agent MAO was adjusted to yield a ratio [Al]:[Ti] of 2000.<br/>
Activities are expressed in kg copolymer per mol of Ti per hour.<br/>
Typical SiMe<sub>3</sub> bands were observed on the infrared spectra at 835; 855 and 1248 cm<sup>-1</sup>.</p>
</description>
<claims id="claims01" lang="en"><!-- EPO <DP n="49"> -->
<claim id="c-en-01-0001" num="0001">
<claim-text>An active catalyst system comprising
<claim-text>a) a metallic complex of formula I
<chemistry id="chem0059" num="0059"><img id="ib0059" file="imgb0059.tif" wi="62" he="67" img-content="chem" img-format="tif"/></chemistry>
wherein R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, R<sub>9</sub>, are each independently selected from hydrogen, unsubstituted or substituted hydrocarbyl having from 1 to 20 carbon atoms, or inert functional group and two or more of those groups can themselves be linked together to form further ring or rings, with the restriction that at least one of R<sub>1</sub>, R<sub>7</sub> and R<sub>8</sub> is not hydrogen;<br/>
wherein M is a metal Group 3 to 10 of the Periodic Table;<br/>
wherein Y is O or NR*, R* being selected from alkyl or aryl having from 1 to 12 carbon atoms;<br/>
wherein each X is the same or different and is selected from halogen, substituted or unsubstituted hydrocarbyl having from 1 to 20 carbon atoms, substituted or unsubstituted aryloxy or alkoxy;<br/>
wherein m is zero or an integer from 1 to 3; and<br/>
wherein (n+1) is the valence of M;</claim-text>
<claim-text>b) an activating agent selected from an aluminium- or boron-containing complex; and<!-- EPO <DP n="50"> --></claim-text>
<claim-text>c) optionally a scavenger and/or a transfer agent.</claim-text></claim-text></claim>
<claim id="c-en-01-0002" num="0002">
<claim-text>The active catalyst system of claim 1 wherein m is zero and R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>9</sub> are the same and are hydrogen.</claim-text></claim>
<claim id="c-en-01-0003" num="0003">
<claim-text>The active catalyst system of claim 1 or claim 2 wherein R<sub>1</sub>, R<sub>7</sub>, R<sub>8</sub> are each independently selected from hydrogen, substituted or unsubstituted hydrocarbyl having from 1 to 20 carbon atoms, halogen, nitro or cyano groups.</claim-text></claim>
<claim id="c-en-01-0004" num="0004">
<claim-text>The active catalyst system of any one of the preceding claims wherein M is Ti, Cr, Zr or Fe.</claim-text></claim>
<claim id="c-en-01-0005" num="0005">
<claim-text>The active catalyst system of any one of the preceding claims wherein X is Cl.</claim-text></claim>
<claim id="c-en-01-0006" num="0006">
<claim-text>A method for preparing the active catalyst system of any one of claims 1 to 5 that comprises the steps of:
<claim-text>a) reacting the ligand of formula II
<chemistry id="chem0060" num="0060"><img id="ib0060" file="imgb0060.tif" wi="65" he="78" img-content="chem" img-format="tif"/></chemistry><!-- EPO <DP n="51"> -->
with a metallic salt MX<sub>n+1</sub> in a solvent, wherein R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, R<sub>9</sub>, M, X, Y, m and n are as described in any one of claims 1 to 5;</claim-text>
<claim-text>b) adding an activating agent having an ionising action and selected from an aluminium- or boron-containing complex or adding an activating support;</claim-text>
<claim-text>c) optionally adding or scavenger and/or a transfer agent;</claim-text>
<claim-text>d) retrieving an active oligomerisation or polymerisation catalyst system</claim-text></claim-text></claim>
<claim id="c-en-01-0007" num="0007">
<claim-text>The method of claim 6 wherein the activating agent is a fluorinated activating support.</claim-text></claim>
<claim id="c-en-01-0008" num="0008">
<claim-text>A method for oligomerising or homo- or co-polymerising ethylene and alpha-olefins that comprises the steps of:
<claim-text>a) injecting the active catalyst system of any one of claims 1 to 5 into the reactor;</claim-text>
<claim-text>b) injecting the monomer and optional comonomer into the reactor either before or after or simultaneously with step a);</claim-text>
<claim-text>c) maintaining under polymerisation conditions;</claim-text>
<claim-text>d) retrieving the oligomers or polymer.</claim-text></claim-text></claim>
<claim id="c-en-01-0009" num="0009">
<claim-text>The method of claim 8 wherein the monomer and optional comonomer are selected from ethylene, propylene and hexene.</claim-text></claim>
<claim id="c-en-01-0010" num="0010">
<claim-text>A polymer obtainable by the method of claim 8 or claim 9.</claim-text></claim>
</claims>
<claims id="claims02" lang="de"><!-- EPO <DP n="52"> -->
<claim id="c-de-01-0001" num="0001">
<claim-text>Aktives Katalysatorsystem, umfassend:
<claim-text>a) einen metallischen Komplex der Formel I
<chemistry id="chem0061" num="0061"><img id="ib0061" file="imgb0061.tif" wi="68" he="73" img-content="chem" img-format="tif"/></chemistry>
wobei R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, R<sub>9</sub> jeweils unabhängig aus Wasserstoff, unsubstituiertem oder substituiertem Hydrocarbyl mit 1 bis 20 Kohlenstoffatomen oder inerter funktioneller Gruppe ausgewählt sind, und wobei zwei oder mehrere dieser Gruppen selbst miteinander verknüpft sein können, um einen weiteren oder weitere Ringe zu bilden, mit der Maßgabe, dass zumindest eines von R<sub>1</sub>, R<sub>7</sub> und R<sub>8</sub> nicht Wasserstoff ist;<br/>
wobei M eine Metallgruppe 3 bis 10 des Periodensystems ist;<br/>
wobei Y O oder NR* ist, wobei R* aus Alkyl oder Aryl mit 1 bis 12 Kohlenstoffatomen ausgewählt ist;<br/>
wobei jedes X gleich oder unterschiedlich und aus Halogen, substituiertem oder unsubstituiertem Hydrocarbyl mit 1 bis 20 Kohlenstoffatomen, substituiertem oder unsubstituiertem Aryloxy oder Alkoxy ausgewählt ist;<br/>
wobei m Null oder eine ganze Zahl von 1 bis 3 ist; und<br/>
wobei (n+1) die Valenz von M ist;</claim-text>
<claim-text>b) ein Aktivierungsmittel, ausgewählt aus einem aluminium- oder borhaltigen Komplex; und</claim-text>
<claim-text>c) optional einen Scavenger und/oder ein Transfermittel.</claim-text></claim-text></claim>
<claim id="c-de-01-0002" num="0002">
<claim-text>Aktives Katalysatorsystem nach Anspruch 1, wobei m Null ist und R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>9</sub> gleich und Wasserstoff sind.<!-- EPO <DP n="53"> --></claim-text></claim>
<claim id="c-de-01-0003" num="0003">
<claim-text>Aktives Katalysatorsystem nach Anspruch 1 oder 2, wobei R<sub>1</sub>, R<sub>7</sub>, R<sub>8</sub> jeweils unabhängig aus Wasserstoff, substituiertem oder unsubstituiertem Hydrocarbyl mit 1 bis 20 Kohlenstoffatomen, Halogen, Nitro oder Cyanogruppen ausgewählt sind.</claim-text></claim>
<claim id="c-de-01-0004" num="0004">
<claim-text>Aktives Katalysatorsystem nach einem der vorstehenden Ansprüche, wobei M Ti, Cr, Zr oder Fe ist.</claim-text></claim>
<claim id="c-de-01-0005" num="0005">
<claim-text>Aktives Katalysatorsystem nach einem der vorstehenden Ansprüche, wobei X Cl ist.</claim-text></claim>
<claim id="c-de-01-0006" num="0006">
<claim-text>Verfahren zum Herstellen des aktiven Katalysatorsystems nach einem der Ansprüche 1 bis 5, das die folgenden Schritte umfasst:
<claim-text>a) Reagieren des Liganden der Formel II
<chemistry id="chem0062" num="0062"><img id="ib0062" file="imgb0062.tif" wi="70" he="84" img-content="chem" img-format="tif"/></chemistry>
mit einem Metallsalz MX<sub>n+1</sub> in einem Lösungsmittel, wobei R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, R<sub>9</sub>, M, X, Y, m und n wie in einem der Ansprüche 1 bis 5 beschrieben sind;</claim-text>
<claim-text>b) Hinzufügen eines Aktivierungsmittels mit ionisierender Wirkung, das aus einem aluminium- oder borhaltigen Komplex ausgewählt ist, oder Hinzufügen eines Aktivierungsträgers;</claim-text>
<claim-text>c) optionales Hinzufügen eines Scavengers und/oder eines Transfermittels;</claim-text>
<claim-text>d) Gewinnen eines aktiven Oligomerisations- oder Polymerisationskatalysatorsystems.</claim-text></claim-text></claim>
<claim id="c-de-01-0007" num="0007">
<claim-text>Verfahren nach Anspruch 6, wobei das Aktivierungsmittel ein fluorierter Aktivierungsträger ist.<!-- EPO <DP n="54"> --></claim-text></claim>
<claim id="c-de-01-0008" num="0008">
<claim-text>Verfahren zum Oligomerisieren oder Homo- oder Copolymerisieren von Ethylen und alpha-Olefinen, das die folgenden Schritte umfasst:
<claim-text>a) Einspritzen des aktiven Katalysatorsystems nach einem der Ansprüche 1 bis 5 in den Reaktor;</claim-text>
<claim-text>b) Einspritzen des Monomers und optionalen Comonomers in den Reaktor entweder vor oder nach oder gleichzeitig mit Schritt a);</claim-text>
<claim-text>c) Halten unter Polymerisationsbedingungen;</claim-text>
<claim-text>d) Gewinnen der Oligomere oder des Polymers.</claim-text></claim-text></claim>
<claim id="c-de-01-0009" num="0009">
<claim-text>Verfahren nach Anspruch 8, wobei das Monomer und das optionale Comonomer aus Ethylen, Propylen und Hexen ausgewählt sind.</claim-text></claim>
<claim id="c-de-01-0010" num="0010">
<claim-text>Polymer, erhältlich mit dem Verfahren nach Anspruch 8 oder 9.</claim-text></claim>
</claims>
<claims id="claims03" lang="fr"><!-- EPO <DP n="55"> -->
<claim id="c-fr-01-0001" num="0001">
<claim-text>Système catalytique actif comprenant
<claim-text>a) un complexe métallique de formule I
<chemistry id="chem0063" num="0063"><img id="ib0063" file="imgb0063.tif" wi="61" he="66" img-content="chem" img-format="tif"/></chemistry>
dans laquelle R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub> et R<sub>9</sub> sont chacun indépendamment choisis parmi un atome d'hydrogène, un groupe hydrocarbyle non substitué ou substitué comportant de 1 à 20 atomes de carbone, ou un groupe fonctionnel inerte, et deux ou plusieurs de ces groupes peuvent eux-mêmes être liés les uns aux autres pour former un ou des noyaux supplémentaires, à condition qu'au moins l'un des radicaux R<sub>1</sub>, R<sub>7</sub> et R<sub>8</sub> ne soit pas un atome d'hydrogène ;<br/>
dans laquelle M représente un métal des Groupes 3 à 10 du Tableau périodique des éléments ;<br/>
dans laquelle Y représente un atome d'O ou un groupe NR*, R* étant choisi parmi un groupe alkyle ou aryle comportant de 1 à 12 atomes de carbone ;<br/>
dans laquelle chaque radical X est identique ou différent et est choisi parmi un atome d'halogène, un groupe hydrocarbyle substitué ou non substitué comportant de 1 à 20 atomes de carbone, un groupe aryloxy substitué ou non substitué ou un groupe alcoxy ;<br/>
dans laquelle m vaut zéro ou un nombre entier de 1 à 3 ; et<br/>
dans laquelle (n + 1) représente la valence de M ;</claim-text>
<claim-text>b) un agent d'activation choisi parmi un complexe contenant de l'aluminium ou du bore ; et<!-- EPO <DP n="56"> --></claim-text>
<claim-text>c) optionnellement un fixateur et/ou un agent de transfert.</claim-text></claim-text></claim>
<claim id="c-fr-01-0002" num="0002">
<claim-text>Système catalytique actif selon la revendication 1 dans lequel m vaut zéro et R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub> et R<sub>9</sub> sont identiques et sont constitués d'un atome d'hydrogène.</claim-text></claim>
<claim id="c-fr-01-0003" num="0003">
<claim-text>Système catalytique actif selon la revendication 1 ou la revendication 2 dans lequel R<sub>1</sub>, R<sub>7</sub> et R<sub>8</sub> sont chacun indépendamment choisis parmi un atome d'hydrogène, un groupe hydrocarbyle substitué ou non substitué comportant de 1 à 20 atomes de carbone, un atome d'halogène, et des groupes nitro ou cyano.</claim-text></claim>
<claim id="c-fr-01-0004" num="0004">
<claim-text>Système catalytique actif selon l'une quelconque des revendications précédentes dans lequel M est du Ti, du Cr, du Zr ou du Fe.</claim-text></claim>
<claim id="c-fr-01-0005" num="0005">
<claim-text>Système catalytique actif selon l'une quelconque des revendications précédentes dans lequel X est du Cl.</claim-text></claim>
<claim id="c-fr-01-0006" num="0006">
<claim-text>Procédé de préparation du système catalytique actif selon l'une quelconque des revendications 1 à 5 qui comprend les étapes consistant à :
<claim-text>a) faire réagir le ligand de formule II
<chemistry id="chem0064" num="0064"><img id="ib0064" file="imgb0064.tif" wi="63" he="76" img-content="chem" img-format="tif"/></chemistry>
avec un sel métallique MX<sub>n+1</sub> dans un solvant, formule dans laquelle R<sub>1</sub>, R<sub>2</sub>, R<sub>3</sub>, R<sub>4</sub>, R<sub>5</sub>, R<sub>6</sub>, R<sub>7</sub>, R<sub>8</sub>, R<sub>9</sub>, M, X, Y, m et n sont tels que décrits dans l'une quelconque des<!-- EPO <DP n="57"> --> revendications 1 à 5 ;</claim-text>
<claim-text>b) ajouter un agent d'activation ayant une action ionisante et choisi parmi un complexe contenant de l'aluminium ou du bore ou ajouter un support d'activation ;</claim-text>
<claim-text>c) optionnellement ajouter un fixateur et/ou un agent de transfert ;</claim-text>
<claim-text>d) récupérer un système catalytique actif d'oligomérisation ou de polymérisation</claim-text></claim-text></claim>
<claim id="c-fr-01-0007" num="0007">
<claim-text>Procédé selon la revendication 6 dans lequel l'agent d'activation est un support d'activation fluoré.</claim-text></claim>
<claim id="c-fr-01-0008" num="0008">
<claim-text>Procédé d'oligomérisation ou d'homo- ou de co-polymérisation d'éthylène et d'alpha-oléfines qui comprend les étapes consistant à :
<claim-text>a) injecter le système catalytique actif selon l'une quelconque des revendications 1 à 5 dans le réacteur ;</claim-text>
<claim-text>b) injecter le monomère et le comonomère optionnel dans le réacteur avant, après ou bien en même temps que l'étape a) ;</claim-text>
<claim-text>c) maintenir dans des conditions de polymérisation ;</claim-text>
<claim-text>d) récupérer les oligomères ou le polymère.</claim-text></claim-text></claim>
<claim id="c-fr-01-0009" num="0009">
<claim-text>Procédé selon la revendication 8 dans lequel le monomère et le comonomère optionnel sont choisis parmi l'éthylène, le propylène et l'hexène.</claim-text></claim>
<claim id="c-fr-01-0010" num="0010">
<claim-text>Polymère pouvant être obtenu par le procédé selon la revendication 8 ou la revendication 9.</claim-text></claim>
</claims>
<drawings id="draw" lang="en"><!-- EPO <DP n="58"> -->
<figure id="f0001" num="1"><img id="if0001" file="imgf0001.tif" wi="165" he="120" img-content="drawing" img-format="tif"/></figure><!-- EPO <DP n="59"> -->
<figure id="f0002" num="2,3"><img id="if0002" file="imgf0002.tif" wi="165" he="227" img-content="drawing" img-format="tif"/></figure><!-- EPO <DP n="60"> -->
<figure id="f0003" num="4"><img id="if0003" file="imgf0003.tif" wi="165" he="120" img-content="drawing" img-format="tif"/></figure>
</drawings>
<ep-reference-list id="ref-list">
<heading id="ref-h0001"><b>REFERENCES CITED IN THE DESCRIPTION</b></heading>
<p id="ref-p0001" num=""><i>This list of references cited by the applicant is for the reader's convenience only. It does not form part of the European patent document. Even though great care has been taken in compiling the references, errors or omissions cannot be excluded and the EPO disclaims all liability in this regard.</i></p>
<heading id="ref-h0002"><b>Patent documents cited in the description</b></heading>
<p id="ref-p0002" num="">
<ul id="ref-ul0001" list-style="bullet">
<li><patcit id="ref-pcit0001" dnum="EP0427696A"><document-id><country>EP</country><doc-number>0427696</doc-number><kind>A</kind></document-id></patcit><crossref idref="pcit0001">[0031]</crossref></li>
<li><patcit id="ref-pcit0002" dnum="EP0277004A"><document-id><country>EP</country><doc-number>0277004</doc-number><kind>A</kind></document-id></patcit><crossref idref="pcit0002">[0031]</crossref></li>
</ul></p>
<heading id="ref-h0003"><b>Non-patent literature cited in the description</b></heading>
<p id="ref-p0003" num="">
<ul id="ref-ul0002" list-style="bullet">
<li><nplcit id="ref-ncit0001" npl-type="s"><article><author><name>GIBSON, V.C.</name></author><author><name>SPITZMESSER, S.K.</name></author><atl/><serial><sertitle>Chem. Rev.</sertitle><pubdate><sdate>20030000</sdate><edate/></pubdate><vid>103</vid></serial><location><pp><ppf>283</ppf><ppl/></pp></location></article></nplcit><crossref idref="ncit0001">[0002]</crossref></li>
<li><nplcit id="ref-ncit0002" npl-type="s"><article><author><name>ISMET, K.</name></author><author><name>FATMA, M.</name></author><author><name>DIG DEM E.</name></author><atl/><serial><sertitle>Journal of Polymer Science: Part A: Polymer Chemistry</sertitle><pubdate><sdate>20040000</sdate><edate/></pubdate><vid>42</vid></serial><location><pp><ppf>2717</ppf><ppl>2724</ppl></pp></location></article></nplcit><crossref idref="ncit0002">[0003]</crossref></li>
<li><nplcit id="ref-ncit0003" npl-type="s"><article><author><name>ASADA, H.</name></author><author><name>HAYASHI, K.</name></author><author><name>NEGORO, S.</name></author><author><name>FUJIWARA, M.</name></author><author><name>MATSUSHITA, T.</name></author><atl/><serial><sertitle>Inorganic Chemistry Communications</sertitle><pubdate><sdate>20030000</sdate><edate/></pubdate><vid>6</vid></serial><location><pp><ppf>193</ppf><ppl>196</ppl></pp></location></article></nplcit><crossref idref="ncit0003">[0003]</crossref></li>
<li><nplcit id="ref-ncit0004" npl-type="s"><article><author><name>BACCHI, A.</name></author><author><name>CARCELLI, M.</name></author><author><name>PELIZZI,C.</name></author><author><name>PELIZZI, G.</name></author><author><name>PELAGATTI, P.</name></author><author><name>UGOLOTTI, S.</name></author><atl/><serial><sertitle>Eur. J. lnorg. Chem.</sertitle><pubdate><sdate>20020000</sdate><edate/></pubdate></serial><location><pp><ppf>2179</ppf><ppl>2187</ppl></pp></location></article></nplcit><crossref idref="ncit0004">[0003]</crossref></li>
<li><nplcit id="ref-ncit0005" npl-type="s"><article><author><name>MATSUI S.</name></author><author><name>FUJITA T.</name></author><atl/><serial><sertitle>Catalysis Today</sertitle><pubdate><sdate>20010000</sdate><edate/></pubdate><vid>66</vid></serial><location><pp><ppf>63</ppf><ppl>73</ppl></pp></location></article></nplcit><crossref idref="ncit0005">[0004]</crossref></li>
</ul></p>
</ep-reference-list>
</ep-patent-document>
